CN109748383A - A kind of triangle helical packing for biofilter - Google Patents
A kind of triangle helical packing for biofilter Download PDFInfo
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- CN109748383A CN109748383A CN201811088947.7A CN201811088947A CN109748383A CN 109748383 A CN109748383 A CN 109748383A CN 201811088947 A CN201811088947 A CN 201811088947A CN 109748383 A CN109748383 A CN 109748383A
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- triangle
- helical packing
- tube body
- biofilter
- filler
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- 238000012856 packing Methods 0.000 title claims abstract description 45
- 239000000945 filler Substances 0.000 claims abstract description 29
- 239000000463 material Substances 0.000 claims abstract description 12
- 241000589902 Leptospira Species 0.000 claims abstract description 7
- 238000001125 extrusion Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 27
- 239000010865 sewage Substances 0.000 abstract description 20
- 230000008569 process Effects 0.000 abstract description 18
- 238000010276 construction Methods 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 230000005484 gravity Effects 0.000 abstract description 4
- 244000005700 microbiome Species 0.000 abstract description 4
- 230000009466 transformation Effects 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 239000000706 filtrate Substances 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- 238000011161 development Methods 0.000 description 5
- 230000018109 developmental process Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 239000012528 membrane Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000003139 buffering effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 230000007269 microbial metabolism Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 239000002033 PVDF binder Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 230000002431 foraging effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000006386 memory function Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- AHEWZZJEDQVLOP-UHFFFAOYSA-N monobromobimane Chemical compound BrCC1=C(C)C(=O)N2N1C(C)=C(C)C2=O AHEWZZJEDQVLOP-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 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
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003466 welding Methods 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
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a kind of triangle helical packings for biofilter, it is the tube body of hollow triangle structure including cross section transverse, tube body axially elongates line direction and is formed leptospira structure clockwise or counterclockwise, and tube body direction of rotation is provided with convex ribs on inboard wall of tube body；By distinctive leptospira structure, the apposition growth for the microorganism that is highly advantageous to makes biomembrane have the great scale of construction, so that biofilter organic loading rate be made to increase substantially；It is small to the hydraulic resistance in all directions, it effectively reduces system and operates normally the energy consumption neutralized in backwash process, pole is not easy to result in blockage；The filling-material structure is stablized, and intensity is high, and stability is good；And because the filler specific gravity is small, head loss is small and also small to the load of supporting plate during the backwash process, reduces capital expenditure；The filler can be used for sewage purifier as biological aerated filter, biological drum, moreover it is possible to be widely used in mentioning in mark transformation for other sewage disposal systems.
Description
Technical field
The present invention relates to technical field of sewage, and in particular to a kind of triangle helical packing for biofilter.
Background technique
Field for the treatment of of water pollution in China, the existing sewage treatment plant's (station) for building up operation, especially at municipal sewage
Factory is managed, is substantially all using traditional activated sludge process and deformation technique, oxidation ditch, SBR, A/O, MBR technique etc., although these
Process effect still or even very well, but in the prevalence of take up a large area, capital expenditure is high, processing load is low, operation is opened
It is dynamic sludge bulking slowly, often occur, the deficiencies of load place be absorbed impact, while process equipment efficiency is low, energy consumption
Height is not able to satisfy the requirement of efficient low energy, therefore for over ten years, and various dirt (useless) water process novel techniques continue to bring out.Mesh
Before for, it is most economical effectively be still biological treatment.It is raw as more and more dirty (useless) water processing establishments put into operation
Object processing technique has become the main method of municipal sewage and organic industrial sewage processing.
Since sewage treatment is mainly the engineering for laying particular emphasis on environmental benefit and social benefit, in construction and actual motion
In the process usually by invest, operational management cost is limited.Especially environment contradiction today for becoming increasingly conspicuous, industrial water pollution
Administering becomes " bottleneck " for restricting many enterprise developments and industry development.So being badly in need of being suitble to the new work of sewage treatment of China's national situation
Skill, thus reduce sewage treatment investment and operating cost, save land used, convenient for management, effluent quality is good.So aeration and biological
The biofilm treatment process of the high load capacities such as filter tank (BAF), tower biological filter is by the national economy and social development to China
And environmental protection has a very important significance.
Biological aerated filter is divided into three regions as one of common bio membrane process from structure: buffering
Water distributing area, supporting layer and filter material layer, exhalant region and effluent trough.Treatment sewage by pipeline flow into buffering water distributing area, sewage to
When upstream passes through filter material layer, by exhalant region and effluent trough by pipeline after the microbial film purified treatment of apposition growth on filtrate
Discharge.The effect for buffering water distributing area is that sewage is made to flow uniformly through filter tank section.Enter filter tank in treatment sewage to rise, while by rousing
Blower air blast simultaneously supplies air (oxygen source) required for microbial film is metabolized into pond by aeration tube.It is grown in micro- on filtrate
Absorption solubility organic pollutant is as nutriment required for its physiological activity from sewage for biomembrane, in the metabolic process
Organic matter is decomposed, so that purifying the sewage.When due to BAF operation to a certain extent due on filtrate biomembrane thicken,
Resistance increases and falling off for aging biomembrane must backwash filtrate, and backwash is using air-water joint backwash.By
The core of this visible BAF technique is bio-carrier (biomembrane), and structure and surface characteristic are biomass (volumetric loading) and fortune
The key factor of row energy consumption.
For the commercially available BAF filtrate as engineer application, the haydite of our common 3~6mm of diameter.By the ball of largest domestic
The spherical shape that the light porous biological ceramic particle factory of shape-Huaqi Environmental protection Science & Tech Development Co Ltd provides is light porous
Biological ceramic particle performance detection index see the table below:
Spherical light porous biological ceramic particle performance detection index (being detected by water treatment filter material inspection center, the Ministry of Construction)
| Title | Parameter | Remarks |
| Bulk density/(g/cm3) | 0.7~0.9 | |
| Apparent density/(g/cm3) | 1.4~1.8 | |
| Percentage of damage/% | ≤0.05 | |
| Wear rate/% | ≤3 | |
| Hydrochloric acid soluble rate/% | ≤2 | 6mol/L hydrochloric acid solution |
| Specific surface area/(cm2/g) | ≥4×104 | |
| Intragranular pore rate/% | >30 | |
| Accumulate porosity/% | >42 |
It finds after actual measurement, actual porosity is more slightly lower than the data that inspection center is detected, and is 39%.According to analysis, due to haydite
The non-uniform reason of size causes porosity to be lower.
For bio membrane process it is important that biofilm thickness and total amount (this is being both bio membrane process
There is good proof in biological rotating disk technique).It can be seen that existing solid ceramic grain filter leads to air water than great, porosity is low
Channel is narrow, and film forming thickness is small, unit volume biomass is small.The hydraulic loading in BAF haydite filter tank are as follows: 4~10m3/m3.h, volume
Load is 3~6/m3.d.Bed easily blocks during biofilm development, needs especially for high concentrated organic wastewater
Very high backwash frequency.We require water inlet to do necessary pretreatment guarantee solid suspension concentration not in engineer application simultaneously
Preferably greater than 60mg/L.
Simultaneously as particle it is small, than great, cause corresponding auxiliary facility at high cost.Pond body needs reinforced concrete construction,
Filter plate needs porous and has very high intensity, so being constructed extremely numerous with precast slab or thick steel plate drilling welding
It is trivial.The instantaneous tolerance and water that air purge, washing and combined water and air backwash filtrate need in the process of running are big, corresponding total pressure
With lift demand height, energy consumption is high, and fan noise is also big.The incomparable advantage of the active sludge of biofilm, but due to
The restriction of filler hinders the extensive use of the biofilms classics technique such as BAF and tower biological filter significantly.
For the MBBR thermopnore particle column developed jointly by KaldnesMijcptek company, Norway and SINTEF research institute
Shape filler, the floating stuffing outer dimension: only, biofilm weight 1.30g/ only, accumulates quantity by 25 × 10mm of Ф, filler weight 1.22g/
Are as follows: 150000/m3.Every cubic metre of biofilm weight is 195Kg/m3, calculated by moisture content 96%, every cubic metre of scattered landfill
Expect biomembrane gross dry weight 7.8Kg.It is calculated by the BOD amount of 1:2, every cubic metre of random packing volumetric loading are as follows: 3.9KgBOD5/
m3.d, if taking B/C=0.5, COD load are as follows: 7.8KgCOD/m3.d.Due to its porous passage aisle structure, as biological filter
It is very big to be stacked with resistance for pond filler, and structural strength is not high, therefore can only use as flowing bed fillers.
Summary of the invention
The purpose of the present invention is to provide a kind of triangle helical packings for biofilter, raw on existing filler to solve
The long biomembrane scale of construction is limited and is easy to the problem of blocking.
The technical scheme to solve the above technical problems is that a kind of triangle helical packing for biofilter,
It is the tube body of hollow triangle structure including cross section transverse, the tube body axially elongates line direction and revolved clockwise or counterclockwise
Turn to form leptospira structure, tube body direction of rotation is provided with convex ribs on the inboard wall of tube body.
Further, the screw pitch of the triangle helical packing is 10mm-40mm.
Further, which is made using integral extrusion molding mode.
Further, which is 20mm-30mm, the triangle helical packing cross section transverse triangle side length
For 10mm-30mm.
Further, which is linear structure.
Further, which is broken line type structure.
Further, which is inner arc linear structure.
Further, which is outer arc linear structure.
Further, which is made of plastic material.
The invention has the following advantages: a kind of triangle helical packing for biofilter provided by the present invention,
By distinctive leptospira structure, the apposition growth for the microorganism that is highly advantageous to, biofilm speed is fast, and biomembrane is made to have the great scale of construction
Bigger volumetric loading, so that biofilter organic loading rate be made to increase substantially；It is cavity structure, in all directions
Hydraulic resistance it is small, effectively reduce system operate normally neutralize backwash process in energy consumption, pole is not easy to result in blockage；This is filled out
Expect stable structure, intensity is high, and stability is good；And because the filler specific gravity is small, head loss is small during the backwash process, to filler branch
The load of board is also small, reduces capital expenditure.The filler is applied widely, in addition to can be used for biological aerated filter, tower life
The occasions such as object filter tank, bio-trickling filter, biological drum can be used as organic exhaust gas for mentioning outside mark transformation for sewage disposal system
The filler of biological purification tower.
Detailed description of the invention
Fig. 1 is schematic structural view of the invention；
Fig. 2 is cross section transverse schematic diagram of the present invention；
Fig. 3 is one schematic diagram of embodiment in the present invention；
Fig. 4 is two schematic diagram of embodiment in the present invention；
Fig. 5 is three schematic diagram of embodiment in the present invention；
Fig. 6 is triangle helical packing preferred size schematic diagram；
Appended drawing reference shown in Fig. 1 to Fig. 6 respectively indicates are as follows: 1- tube body, 2- convex ribs, 3- hollow triangle.
Specific embodiment
The principle and features of the present invention will be described below with reference to the accompanying drawings, and the given examples are served only to explain the present invention, and
It is non-to be used to limit the scope of the invention.
As shown in Figure 1 and Figure 2, a kind of triangle helical packing for biofilter, including cross section transverse are hollow triangle
The tube body 1 of 3 structures, tube body 1 axially elongate line direction and are formed leptospira structure clockwise or counterclockwise, in tube body 1
1 direction of rotation of tube body is provided with convex ribs 2 on wall.
The whole structure in the shape of a spiral of triangle helical packing, internal is the cavity of triangular section, and it is attached to be conducive to microorganism
Growth, so that biomembrane is had the great scale of construction, so that biofilter organic loading rate be made to increase substantially；And triangle has pole
Strong stability can effectively reinforce integrally-built stability.The helical packing due to being not easy to result in blockage for cavity structure,
Keep the water body resistance in all directions small, reduces system and operate normally the energy consumption neutralized in backwash process.When triangle spiral
Filler is in accumulation in biological aerated filter in use, only point contact or extremely short line connects between adjacent triangle helical packing
Touching, does not easily cause the damage of biomembrane in triangle helical packing.Convex ribs 2 are arranged on three faces in triangular pipe bodies 1, each
One is provided on face, setting is spiral along 1 direction of rotation of tube body, and the height of preferred convex ribs 2 is 1.8mm, triangle spiral shell
Filler surface is revolved with a thickness of 0.8mm.In the shape of a spiral due to convex ribs 2, when there is sewage to pass through, sewage is effectively prevented to raw
The biomembrane generation of long attachment is excessive to wash away, the structural strength of this structure effective enhancing triangle helical packing simultaneously.
It is also other linear structures that the triangle helical packing cross section transverse three sides of a triangle, which can be linear structure,；
In general, the cross section transverse of triangle helical packing is triangular structure or belongs to protection of the present invention similar to the structure of triangle
Range.
Embodiment one, as shown in figure 3, the triangle helical packing cross section transverse three sides of a triangle are broken line type knot
Structure.
Embodiment two, as shown in figure 4, the triangle helical packing cross section transverse three sides of a triangle are interior arc line type knot
Structure.The interior arc line type is arc line type of the side to helical packing center dimpling.
Embodiment three, as shown in figure 5, the triangle helical packing cross section transverse three sides of a triangle are outer arc line type knot
Structure.The outer arc line type is arc line type of the side to dimpling on the outside of helical packing.
In conclusion shifting gears can by the triangular shaped change to the triangle helical packing cross section transverse
By adjusting the degree of convexity of broken line, camber line outwardly or inwardly, to effectively control the internal channel after triangle helical packing is piled up
It is suitable to effectively increase the triangle helical packing to adapt to the different application condition in engineer application with the hole ratio of outer tunnel
Use range.
In the present invention, the hollow triangle circumscribed circle diameter of the preferred triangle helical packing cross section transverse is 14mm, axis
Line direction length is 20mm.Its performance parameter is as shown in the table:
| Title | Parameter | Remarks |
| Bulk density/(g/cm3) | About 0.15 | Dissipate heap |
| Apparent density/(g/cm3) | About 0.95 | Dissipate heap |
| Percentage of damage/% | 0 | |
| Wear rate/% | 0 | |
| Effective biofilm area/(m2/m3) | ≥387 | Dissipate heap |
| Accumulate overall porosity/% | ≥85 | Dissipate heap |
| Interior porosity/% | About 27 | Inside is effective biofilm surface |
| External pores rate/% | About 58 | Outside is effective biofilm surface |
It is 1mm by biofilm thickness under aerobic condition, moisture content 96% calculates, and can obtain aerobic biologic membrane dry weight 40g/m2,
Every cubic metre of random packing biomembrane gross dry weight 15.48Kg.It is calculated by the BOD amount of 1:1, BOD loading maximum value is 40g/m2.d,
By break value 0.02KgBOD5/m2.d it calculates, every cubic metre of random packing volumetric loading are as follows: 7.74KgBOD5/m3.d, if taking B/C
=0.5, then COD load are as follows: 15.48KgCOD/m3.d.Overall porosity is down to 55% by 85% after biofilm, only calculates inside filler
Porosity after biofilm is 53%.For microbial metabolism provide mass exchange and aging demoulding channel, may be allowed into
Water has higher solid suspension concentration.
There are also intensity height, easy the characteristics of stacking in addition to the feature that porosity is high, effective biofilm area is big for the filler.Main body is disconnected
The triangle helical structure in face has extremely strong stability, on the one hand internal convex ribs increase the intensity of filler, another aspect spiral
Body is to protect well to biomembrane.Also there is the filler spring-like " memory function " can restore shape rapidly after becoming compressed simultaneously
Shape.The internal void still having after biofilm forms good channel, is the advantage of microbial metabolism and exterior materials exchange.
In addition helical structure makes the phenomenon that being only point contact or the contact of extremely short line between filler, being not in channel, and resistance to water-flow phase
When small.
Since filler bulk density is minimum, the biofilter BAF can be such that equipmentization flexibly uses.No matter pond body or filter plate add
Work production is all very easy to, and can further decrease occupied area.The corresponding total pressure of blower and water pump and lift of backwash
Also it can greatly reduce, energy saving.
For save the cost, it is convenient to make, and in the present invention, which uses integral extrusion molding mode system
?.Had using extrusion mould special, the material of use is mixed and is used extruder and extrusion die cooperate extrusion molding, be crowded
It is molded as one formula structure out, strengthens the intensity of helical packing, prolongs the service life.
In order to play the superiority of helical packing, in the present invention, according to the needs of use, which can be cut
For different length, such as the various length of 10mm, 15mm, 25mm, it is preferred that triangle helical packing length is 20mm-30mm, is applicable in
In most of occasion, and a length of 10mm-30mm of the triangle helical packing cross section transverse triangle edges.
In the present invention, which is made of plastic material, which includes PP, PE, PVC, PVDF etc.；
Its making material is extensive, and it is convenient to draw materials, and can easily use extrusion molding；And specific gravity is 0.95 or so, lighter in weight.
The above are a specific embodiment of the invention, from implementation process as can be seen that one kind provided by the present invention is used for
The triangle helical packing of biofilter passes through distinctive leptospira structure, the apposition growth for the microorganism that is highly advantageous to, biofilm speed
Fastly, biomembrane is made to have the great scale of construction and bigger volumetric loading, so that biofilter organic loading rate be made to increase substantially；Its
Small to the hydraulic resistance in all directions for cavity structure, the system that effectively reduces operates normally in neutralization backwash process
Energy consumption, pole are not easy to result in blockage；The filling-material structure is stablized, and intensity is high, and stability is good；And because the filler specific gravity is small, backwashing
Head loss is small in the process, also small to the load of supporting plate, reduces capital expenditure.The filler is applied widely, in addition to
It can be used for the occasions such as biological aerated filter, tower biological filter, bio-trickling filter, biological drum, for mentioning for sewage disposal system
Mark transformation is outer, can be used as the filler of organic exhaust gas biological purification tower.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all in spirit of the invention and
Within principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.
Claims (9)
1. a kind of triangle helical packing for biofilter, which is characterized in that including cross section transverse be hollow triangle (3) knot
The tube body (1) of structure, the tube body (1) axially elongate line direction and are formed leptospira structure clockwise or counterclockwise, institute
It states and tube body (1) direction of rotation is provided with convex ribs (2) on inboard wall of tube body.
2. a kind of triangle helical packing for biofilter according to claim 1, which is characterized in that the triangle spiral
The screw pitch of filler is 10mm-40mm.
3. a kind of triangle helical packing for biofilter according to claim 2, which is characterized in that the triangle spiral
Filler is made using integral extrusion molding mode.
4. a kind of triangle helical packing for biofilter according to claim 3, which is characterized in that the triangle spiral
Pack length is 20mm-30mm, a length of 10mm-30mm of the triangle helical packing cross section transverse triangle edges.
5. a kind of triangle helical packing for biofilter according to claim 3, which is characterized in that the triangle spiral
Filler cross section transverse three sides of a triangle are linear structure.
6. a kind of triangle helical packing for biofilter according to claim 3, which is characterized in that the triangle spiral
Filler cross section transverse three sides of a triangle are broken line type structure.
7. a kind of triangle helical packing for biofilter according to claim 3, which is characterized in that the triangle spiral
Filler cross section transverse three sides of a triangle are inner arc linear structure.
8. a kind of triangle helical packing for biofilter according to claim 3, which is characterized in that the triangle spiral
Filler cross section transverse three sides of a triangle are outer arc linear structure.
9. a kind of triangle helical packing for biofilter according to any one of claims 1 to 8, which is characterized in that
The triangle helical packing is made of plastic material.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201811088947.7A CN109748383A (en) | 2018-09-18 | 2018-09-18 | A kind of triangle helical packing for biofilter |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201811088947.7A CN109748383A (en) | 2018-09-18 | 2018-09-18 | A kind of triangle helical packing for biofilter |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113860485A (en) * | 2021-11-03 | 2021-12-31 | 河南省科学院能源研究所有限公司 | Suspended biological filler |
| CN115745234A (en) * | 2022-11-01 | 2023-03-07 | 同济大学建筑设计研究院(集团)有限公司 | Multi-medium composite filling water treatment system and using method thereof |
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| CN104787874A (en) * | 2015-04-08 | 2015-07-22 | 大连爱特流体控制有限公司 | Multi-phase flow dynamic membrane microbial carrier filler |
| KR20170016126A (en) * | 2015-08-03 | 2017-02-13 | 주식회사 홍익기술단 | Microbe Carrier and Method for Wastewater Treatment |
| CN209276220U (en) * | 2018-09-18 | 2019-08-20 | 成都利尔环保技术开发有限公司 | A kind of triangle helical packing for biofilter |
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| CN113860485A (en) * | 2021-11-03 | 2021-12-31 | 河南省科学院能源研究所有限公司 | Suspended biological filler |
| CN115745234A (en) * | 2022-11-01 | 2023-03-07 | 同济大学建筑设计研究院(集团)有限公司 | Multi-medium composite filling water treatment system and using method thereof |
| CN115745234B (en) * | 2022-11-01 | 2023-07-04 | 同济大学建筑设计研究院(集团)有限公司 | Multi-medium composite filling water treatment system and application method thereof |
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