CN209143818U - ceramic flat plate film structure - Google Patents
ceramic flat plate film structure Download PDFInfo
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- CN209143818U CN209143818U CN201821947812.7U CN201821947812U CN209143818U CN 209143818 U CN209143818 U CN 209143818U CN 201821947812 U CN201821947812 U CN 201821947812U CN 209143818 U CN209143818 U CN 209143818U
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- Prior art keywords
- plate ontology
- earthenware slab
- flat plate
- membrane structure
- plate body
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- 239000000919 ceramic Substances 0.000 title claims abstract description 8
- 239000012528 membrane Substances 0.000 claims abstract description 84
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 238000007789 sealing Methods 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 239000002351 wastewater Substances 0.000 claims abstract description 6
- 229910052571 earthenware Inorganic materials 0.000 claims description 36
- 239000004927 clay Substances 0.000 claims description 15
- 239000011148 porous material Substances 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 239000011159 matrix material Substances 0.000 claims description 4
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical group [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 3
- 239000002390 adhesive tape Substances 0.000 claims description 3
- 239000004568 cement Substances 0.000 claims description 3
- 239000002131 composite material Substances 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims description 3
- 229910052717 sulfur Inorganic materials 0.000 claims description 3
- 239000011593 sulfur Substances 0.000 claims description 3
- 238000011049 filling Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 10
- 239000008235 industrial water Substances 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000004891 communication Methods 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 239000010409 thin film Substances 0.000 description 18
- 238000010586 diagram Methods 0.000 description 15
- 239000010408 film Substances 0.000 description 12
- 239000004698 Polyethylene Substances 0.000 description 10
- 229920000573 polyethylene Polymers 0.000 description 9
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 9
- 239000012510 hollow fiber Substances 0.000 description 8
- -1 polyethylene Polymers 0.000 description 7
- 239000002033 PVDF binder Substances 0.000 description 6
- 229920002492 poly(sulfone) Polymers 0.000 description 5
- 229920002239 polyacrylonitrile Polymers 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000004065 wastewater treatment Methods 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- 150000003457 sulfones Chemical class 0.000 description 4
- 229920003002 synthetic resin Polymers 0.000 description 4
- 239000000057 synthetic resin Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 150000001336 alkenes Chemical class 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- PQIOSYKVBBWRRI-UHFFFAOYSA-N methylphosphonyl difluoride Chemical group CP(F)(F)=O PQIOSYKVBBWRRI-UHFFFAOYSA-N 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000002146 bilateral effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 231100000481 chemical toxicant Toxicity 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000009432 framing Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a dull and stereotyped film structure of pottery is applicable to and handles running water, industrial water, processing procedure solid-liquid separation, waste water and water recovery, a serial communication port, include: the water flow pipe comprises a first flat plate body, a second flat plate body, a sealing element arranged between the first flat plate body and the second flat plate body, and at least one water flow pipe; the first flat plate body and the second flat plate body are respectively ceramic flat plates with a plurality of holes, and the first flat plate body and/or the second flat plate body are/is provided with a filter membrane; the sealing element is arranged in the gap between the first flat plate body and the second flat plate body and is provided with at least one through hole; the inner space between the first flat plate body and the second flat plate body is provided with a plurality of flow guide elements to form a liquid flow channel.
Description
Technical field
A kind of earthenware slab membrane structure of the utility model about water treatment technology, particularly relates to a kind of high efficiency, can
Filter bacteria and the small earthenware slab membrane structure of occupied area.
Background technique
In recent years, due to the enhancing of environmental consciousness, processing for trade waste and domestic refuse or again
It utilizes, extraordinarily by the attention of general public.For example: exhaust gas, waste water, solid waste or toxic chemicals etc. are numerous
Processing, the disposition of waste material etc. among, industrial water, discharge water or be considerable with related wastewater treatment of living
As soon as ring, if effluent sewage not only endangers the ecological balance of nature, but also also may be used not by processing appropriate arbitrarily discharge
Water resource, which can be destroyed, causes the scarcity of domestic water insufficient, or even will be sizable to the generation of entire environment during extremely short
It threatens and destroys.
Traditional wastewater treatment process or method mainly removes the floating material and suspended solid in water removal in advance, then adds again
Add the inorganic matter in Chemical treatment water or utilize the organic matter in biological decomposition water, is finally further carried out subsequent
Processing or advanced processes so as to meet release water water quality discharge standard or regeneration water standard.
The method or means of common subsequent processing or advanced processes include fine sieve, filtering, oxidation, active carbon and inverse
The technologies such as infiltration.Level is required however, being only capable of reaching general using these common programs processing sewage, but can not often be expired
The high standards of sufficient residence resident and green group to ambient water quality.
Therefore, it is difficult to meet increasingly strict effluent-disposal standard to improve common processing technique, utilizes film mistake
Filter combines the processing method of the thin-film bioreactor (Membrane bioreactor, MBR) of biological treatment just to come into being
And becoming the processing technique being widely adopted often, there are four types of types for the thin film bio reaction mould group of common business or non-commercialization
Formula: (1) flat thin-film bioreactor, (2) tubular membranes bioreactor, (3) spiral thin-film bioreactor and (4)
Hollow fiber form thin-film bioreactor, and film material then includes polyvinylidene fluoride (Polyvinylidene
Difluoride, PVDF), it is polyethylene (Polyethylene, PE), polyethylene sulfone (Polyethylsulfone, PES), poly-
Sulfone (Polysulfone, PS) and polyacrylonitrile (Polyacrylonitrile, PAN) etc..
However, common four kinds of thin film bios react mould group at present, it is respectively present following disadvantage (1) flat thin film bio
Reactor: it since every thin film in the flat thin-film bioreactor of organic material is required to an other supporting layer, causes
Keep packed density and solids interdiction capability bad, and film not easy cleaning, replacement, when Yu Qingxi, replacement is easy to damaged.
(2) tubular membranes bioreactor: since the packed density of tubular membranes bioreactor is minimum, solid is intercepted
The ability of object is preferable, and can operate under high pressure, can also be cleaned using physical mode, still, unit area film
Required space is more, and larger in the pressure loss, causes operation at opposite raising.
(3) screw thin-film bioreactor: though spiral thin film bioreactor packed density with higher, is limited to
Simple structure and keep its solids interdiction capability worst, it is more difficult for the control of concentration polarization, and not easy cleaning.
(4) hollow fiber form thin-film bioreactor: packed density is high the characteristics of hollow fiber form thin-film bioreactor,
Can back flush, though manufacturing cost is low with the more flat thin-film bioreactor of consuming energy, since waterpower and dynamic environment are not easy
Control, is also easy to produce incrustation, causes to clean frequent problem.
In addition, the flat filter membrane used by thin-film bioreactor is (also known as flat for waste water treatment efficiency
Plate film) considerable role is played, it is one of the key factor for determining entire waste water treatment system success or not often.°
But common hollow fiber membrane (PVDF material), synthetic resin plate membrane (PVDF, PD material) still have now
Obvious disadvantage, such as: (1) heat resistance is low, and temperature can not be higher than 50 DEG C；(2) service life is short, the service life of hollow fiber membrane
About 3~5 years, service life about 5~7 years of synthetic resin plate membrane；(3) obstructing problem, the membrane tube seam crossing of hollow fiber membrane and inner edge
It is easy to obstruction and fracture of wire, synthetic resin plate membrane back washing pressure is small and is easy to block；(4) environmental issue, hollow fiber membrane and synthesis
Resinous flat film is not easily recycled recycling.
Thus, all circles there's no one who doesn't or isn't urgently develop a kind of thin-film bioreactor, are not only able to solve above-mentioned conventional films life
The problem of object reactor, has been also equipped with the advantages that heat-resisting, oil removing, antiblocking and cleaning are easy, has allowed industry can be more efficiently
Ground carries out Industrial Wastewater Treatment and recycling.
Utility model content
According to above situation, the present inventor proposes the innovation structure that flat thin-film bioreactor is improved with ceramic material
Think, improve flat thin-film bioreactor heat resistance be low in use, service life is short, obstruction, environmental protection the problems such as.
Also that is, the utility model provides a kind of earthenware slab membrane structure, at water treatment, industrial water
Reason, processing procedure be separated by solid-liquid separation, waste water and water recycling comprising: the first plate ontology configures in opposite directions with the first plate ontology
Second plate ontology, the sealing element being set between the first plate ontology and the second plate ontology and at least one
A flow tube；Wherein the first plate ontology and the second plate ontology are respectively the ceramic flat with multiple holes
Plate, and an at least side surface for the first plate ontology and/or the second plate ontology has filter membrane；It is described close
Envelope element is to be disposed in the first plate ontology and the interstitial spaces of the second plate ontology are formed by sealing state
Sealing portion, and the sealing element is provided at least one through hole；The first plate ontology and the second plate ontology
Between inner space be provided with multiple diversion members, and assortment, at the matrix array arranged in N row * M, wherein N, M are respectively and are greater than
Or the natural number equal to 1, to form liquid flow path；And the flow tube is interconnected to form with the through hole
Fluid connection.
To solve the problems, such as aforementioned conventional flat filter membrane, such as: the organic films such as hollow fiber membrane, synthetic resin plate membrane,
Therefore the first plate ontology of the utility model and the second plate ontology Ceramics material are made, due to ceramic material
Have oil resistivity it is heat-resisting up to 80 DEG C, service life up to 10~15 years so that reduce life cycle cost, be also equipped with back washing
Pressure is not easy the advantages that blocking, if diaphragm blocks, can restore pressure difference by high-pressure wash dirt of making a return journey, effectively
The shortcomings that improving the prior art, is particularly suited for industrial water drainage, public be lauched leads, the front-end processing of sea water desalination RO system, has
It is a variety of that film separated activated sludge in the fields such as the resource reclaim of valence object is handled, net solid and reclaimed wastewater reuse etc. are hanged in removal
Purposes.
An implementation form according to the present utility model, wherein the sealing element with a thickness of 5~20mm.
An implementation form according to the present utility model further has an at least protection portion, is fixedly arranged on described first
The long side outer rim of plate ontology or the second plate ontology.
An implementation form according to the present utility model, wherein the sealing element is constrictive type clay, insulated enclosure item, fills out
Adhesive tape, ceramics modeling at least one of item and bonding cement are stitched, wherein constrictive type clay is that silicate clay or Sulfur clay are viscous
Native clay.
An implementation form according to the present utility model, wherein the inside and/or outside of the sealing element are further provided with
An at least waterproof ventilated membrane.
An implementation form according to the present utility model, wherein the diversion trench is longitudinal arrangement, transversely arranged and oblique row
At least one of column.
An implementation form according to the present utility model, wherein the flow tube is metallic water pipe, plastic water pipe and compound
At least one of water pipe.
An implementation form according to the present utility model, wherein the first plate ontology and the second plate ontology is flat
Equal aperture is 0.05 μm~3.5 μm.
An implementation form according to the present utility model, wherein the average pore size of the filter membrane is 0.1 μm~3.5 μm.
An implementation form according to the present utility model, wherein the effective filtration area of the filter membrane is 0.1m2/ monolithic~
1.5m2/ monolithic.
An implementation form according to the present utility model, wherein the filter membrane is organic polymer, to gather inclined difluoro second
Alkene PVDF (Polyvinylidene difluoride), polythene PE (polyethylene), polyethylene sulfone
(Ployethylsulfone), at least one in polysulfones (Polysulfone) and polyacrylonitrile (Ployacrylonitrile)
Kind material is constituted.
Hereinafter, each diagram referring to appended by the utility model specification, for the purpose of this utility model and reach effect,
And the features such as the composition element of earthenware slab membrane structure disclosed in the utility model, construction are described in detail.
Detailed description of the invention
Fig. 1 is the schematic diagram of the earthenware slab membrane structure of an embodiment of the utility model.
Fig. 2 is the flow path schematic diagram of the earthenware slab membrane structure of an embodiment of the utility model.
Fig. 3 is the partial enlargement diagram of the earthenware slab membrane structure of an embodiment of the utility model.
Fig. 4 is the schematic diagram of the earthenware slab membrane structure of another embodiment of the utility model.
Fig. 5 is the partial enlargement diagram of the earthenware slab membrane structure of another embodiment of the utility model.
Fig. 6 is the schematic diagram of the earthenware slab membrane structure of another embodiment of the utility model.
Fig. 7 is the schematic diagram of the earthenware slab membrane structure of another embodiment of the utility model.Wherein: 1: earthenware slab
Membrane structure；10: the first plate ontologies；11: filter membrane；20: the second plate ontologies；30: sealing element；31: waterproof ventilated membrane；
40: diversion member；41: liquid flow path；50: flow tube；60: protection portion.
Specific embodiment
Hereinafter, constituted for the utility model and technology contents etc., enumerate various applicable examples and cooperate referring to
Literary institute's accompanying drawings and explained in detail；However, the utility model be of course not defined in the cited grade embodiment,
Schema or detailed description.
Furthermore it should be understood by those skilled in the art that: cited embodiment and appended schema only provide and refer to and say
It is bright to be used, not it is used to limit the utility model；Can be easy the modification implemented or change based on equal record and
The creation of completion is also all considered as in the range of the spirit and intention for not departing from the utility model, and certain grade creation also include
In the claim of the utility model.
Firstly, please referring to Fig. 1.Earthenware slab membrane structure in one embodiment of the utility model as shown in Figure 1
Schematic diagram comprising: the first plate ontology 10, the second plate ontology 20 configured in opposite directions with the first plate ontology, setting
Sealing element 30 and at least one flow tube 50 between the first plate ontology and the second plate ontology；Its
Described in the first plate ontology 10 and the second plate ontology 20 be respectively the earthenware slab with multiple holes, and it is described
An at least side surface for first plate ontology 10 and/or the second plate ontology 20 has filter membrane 11；The sealing element
30 be to be disposed in the first plate ontology 10 and the interstitial spaces of the second plate ontology 20 are formed by sealing state
Sealing portion, and the sealing element 30 is provided at least one through hole；The first plate ontology and the second plate sheet
Inner space between body is provided with multiple diversion members 40, and assortment, at the matrix array arranged in N row * M, wherein N, M are respectively
Natural number more than or equal to 1, to form liquid flow path 41；And the flow tube 50 and the through hole it is mutual
Connection forms fluid connection.
Please refer to Fig. 2.The flow path of the earthenware slab membrane structure of one embodiment of the utility model as shown in Figure 2
Schematic diagram, in the present embodiment, the diversion member 40 are set to the 10 or described second plate ontology of the first plate ontology
On 20 medial surface, and with assortment at equal intervals at the matrix array in 5 row * 2 column；When by negative pressure device (not shown) from described in
When the flow tube 50 of the through hole of the surrounding of sealing element 30 provides negative pressure extracting, waste water and sewage can be promoted from described the
One plate ontology 10 and the second plate ontology 20 penetrate into, and guide and shunt further in accordance with the diversion member 40, so that the pottery
Liquid in porcelain flat sheet membranes structure is flowed out in a manner of low discharge via the flow tube 50, wherein the diversion member 40
Permutation and combination can be realized using any mode well-known to those skilled in the art, such as: longitudinal arrangement, it is transversely arranged and
At least one of arranged askew, and the utility model does not make especially to limit for the arrangement of the diversion trench.
Please refer to Fig. 3.The partial enlargement of the earthenware slab membrane structure of one embodiment of the utility model as shown in Figure 3
Schematic diagram, wherein the surface of the first plate ontology 10 and the second plate ontology 20 has filter membrane 11；The sealing
The inside and outside of element 30 are equipped with waterproof ventilated membrane 31；Wherein the sealing element 30 with a thickness of 5~20mm；It is described
Sealing element 30 be constrictive type clay, insulated enclosure item, joint filling adhesive tape, ceramics modeling at least one of item and bonding cement,
Middle constrictive type clay is silicate clay or Sulfur clay puddle clay.
Please refer to Fig. 4 and Fig. 5.Earthenware slab film in another embodiment of the utility model as shown in Figures 4 and 5
The schematic diagram and partial enlargement diagram of structure further have an at least protection portion 60, are fixedly arranged on first plate
The long side outer rim of ontology 10 or the second plate ontology 20, the protection portion 60 is rigid material, in this example the guarantor
Shield portion 60 is strip, and but not limited to this, and the protection portion 60 is to by the first plate ontology and second plate
Ontology frames, and increases the earthenware slab film by framing the 10 or described second plate ontology 20 of the first plate ontology
1 inner tensions of structure and related stress, the protection portion 60 can be unilateral setting or bilateral setting, be double in the present embodiment
Side setting.
Please refer to Fig. 6.The schematic diagram of the earthenware slab membrane structure of another embodiment as shown in FIG. 6, wherein described close
The surrounding of envelope element 30 further has two through holes, and the through hole can be set in the earthenware slab membrane structure
Same side or different a side, in the present embodiment, the through hole is set to same side, and every pass through aperture is set
There is the flow tube 50 for collecting recycle-water, the flow tube 50 is in metallic water pipe, plastic water pipe and composite water pipe
At least one.
Please refer to Fig. 7.The schematic diagram of the earthenware slab membrane structure of another embodiment as shown in Figure 7, wherein described close
The surrounding of envelope element 30 further has there are three through hole, and the through hole can be set in the earthenware slab membrane structure
Same side or different a side, in the present embodiment, the through hole is set to same side, and every pass through aperture is set
There is the flow tube 50 for collecting recycle-water, the flow tube 50 is in metallic water pipe, plastic water pipe and composite water pipe
At least one.
Technical idea according to the present utility model, wherein the first plate ontology 10 and the second plate ontology 20
Average pore size is 0.05 μm~3.5 μm.
Technical idea according to the present utility model, wherein the average pore size of the filter membrane 11 is 0.1 μm~3.5 μm.Institute
The average pore size for stating filter membrane 11 can be 0.2 μm to 3.0 μm.The average pore size of the filter membrane 11 also can be 0.3 μm to 2.5 μ
m.The average pore size of the filter membrane 11 also can be 0.4 μm to 2.0 μm.The average pore size of the filter membrane 11 is preferably 0.5 μm
To 1.5 μm.The average pore size of the filter membrane 11 is more preferably 0.5 μm to 1.0 μm.
Technical idea according to the present utility model, wherein the effective filtration area of the filter membrane 11 is 0.1m2/ monolithic~
3.5m2/ monolithic.The effective filtration area of the filter membrane 11 is preferably 0.1m2/ monolithic is to 2.0m2/ monolithic.The filter membrane 11
Effective filtration area be more preferably 0.2m2/ monolithic is to 1.5m2/ monolithic.The effective filtration area of the filter membrane 11 is particularly good to be
0.3m2/ monolithic is to 0.5m2/ monolithic.
Wherein, the membrane flux of the filter membrane 11 is 0.25~1.2m3/d/m2(stere/square centimeter-day).Institute
The membrane flux for stating filter membrane 11 is preferably 0.35~1.1 m3/d/m2(stere/square centimeter-day).The filter membrane 11
Membrane flux is more preferably 0.45~1.0m3/d/m2(stere/square centimeter-day).The membrane flux of the filter membrane 11 is particularly good to be
0.55~0.9m3/d/m2(stere/square centimeter-day).
Technical idea according to the present utility model, wherein the filter membrane 11 is organic polymer, to gather inclined difluoro second
Alkene PVDF (Polyvinylidene difluoride), polythene PE (polyethylene), polyethylene sulfone
(Ployethylsulfone), at least one in polysulfones (Polysulfone) and polyacrylonitrile (Ployacrylonitrile)
Kind material is constituted.
Finally, the earthenware slab membrane structure of the utility model is used in water processing filtering system, can not only send out
The effect of the processing of earthenware slab membrane structure is waved, with effective cleaning plate film filter-plate structure, can also increase what it was used
Service life, and maintain the effect of water purification.
In summary the explanation and illustration of embodiment, may validate that can provide a kind of ceramic flat according to the utility model
Plate membrane structure also has high patience, high intensity, high reliability, longevity other than the common defect that can improve the prior art
Length is ordered, space is saved, is energy saving, saving and the multiple advantage such as maintain length and can be recycled.
More than, although the content of the utility model, this reality are described in detail with embodiment citing as above
These embodiments are not only defined in novel.It should be understood by those skilled in the art that: do not departing from the utility model
Spirit and scope in, when various change and modification can be carried out again；For example, by each technology illustrated by previous embodiment
Appearance is combined or changes and becomes new embodiment, these embodiments are also considered as the affiliated content of the utility model certainly.
Therefore, the range to be protected of this case also includes aftermentioned claims and its range that is defined.
Claims (10)
1. a kind of earthenware slab membrane structure, be suitable for processing waste water characterized by comprising the first plate ontology, with it is described
The second plate ontology that first plate ontology configures in opposite directions, be set to the first plate ontology and the second plate ontology it
Between sealing element and at least one flow tube；Wherein
The first plate ontology and the second plate ontology are respectively the earthenware slab with multiple holes, and described the
An at least side surface for one plate ontology and/or the second plate ontology has filter membrane；
The sealing element is to be disposed in the first plate ontology and the interstitial spaces of the second plate ontology are formed by
The sealing portion of sealing state, and the sealing element is provided at least one through hole；
Inner space between the first plate ontology and the second plate ontology is provided with multiple diversion members, and assortment at
In the matrix array that N row * M is arranged, wherein N, M are respectively the natural number for being greater than or equal to 1, to form liquid flow path；With
And
The flow tube and the through hole are interconnected to form fluid connection.
2. earthenware slab membrane structure according to claim 1, which is characterized in that the first plate ontology and described second
The distance between plate ontology is 5~20mm.
3. earthenware slab membrane structure according to claim 1, which is characterized in that further there is an at least protection portion,
It is fixedly arranged on the long side outer rim of the first plate ontology or the second plate ontology.
4. earthenware slab membrane structure according to claim 1, which is characterized in that the sealing element be constrictive type clay,
Insulated enclosure item, joint filling adhesive tape, ceramics modeling at least one of item and bonding cement material are constituted, wherein constrictive type clay
It is silicate clay or Sulfur clay puddle clay.
5. earthenware slab membrane structure according to claim 1, which is characterized in that the inside of the sealing element and/or outer
Side is further provided with an at least waterproof ventilated membrane.
6. earthenware slab membrane structure according to claim 1, which is characterized in that the diversion member is longitudinal arrangement, cross
To at least one of arrangement and arranged askew.
7. earthenware slab membrane structure according to claim 1, which is characterized in that the flow tube is metallic water pipe, modeling
Expect at least one of water pipe and composite water pipe.
8. earthenware slab membrane structure according to claim 1, which is characterized in that the first plate ontology and described second
The average pore size of plate ontology is 0.05 μm~3.5 μm.
9. earthenware slab membrane structure according to claim 1, which is characterized in that the average pore size of the filter membrane is 0.1 μ
M~1.0 μm.
10. earthenware slab membrane structure according to claim 1, which is characterized in that the effective filtration area of the filter membrane
For 0.1m2/ monolithic~3.5m2/ monolithic.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW107213392U TWM576074U (en) | 2018-10-02 | 2018-10-02 | Ceramic flat plate film structure |
| TW107213392 | 2018-10-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209143818U true CN209143818U (en) | 2019-07-23 |
Family
ID=66997444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821947812.7U Active CN209143818U (en) | 2018-10-02 | 2018-11-23 | ceramic flat plate film structure |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN209143818U (en) |
| TW (1) | TWM576074U (en) |
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2018
- 2018-10-02 TW TW107213392U patent/TWM576074U/en unknown
- 2018-11-23 CN CN201821947812.7U patent/CN209143818U/en active Active
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| TWM576074U (en) | 2019-04-01 |
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