CN106904743A - A kind of water-treatment biological membrane reactor - Google Patents
A kind of water-treatment biological membrane reactor Download PDFInfo
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- CN106904743A CN106904743A CN201710277670.1A CN201710277670A CN106904743A CN 106904743 A CN106904743 A CN 106904743A CN 201710277670 A CN201710277670 A CN 201710277670A CN 106904743 A CN106904743 A CN 106904743A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
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Abstract
The present invention relates to a kind of water-treatment biological membrane reactor, it is main to be made up of with the attachment for sticking to matrix surface matrix, matrix is plane mesh structure, expanded after the attachment water suction of matrix surface the filling of matrix mesh is formed into water completely can not the film that can diffuse through of directly penetrating but Organic substance in water, the size of matrix mesh is less than or equal to critical dimension, critical dimension is mesh just by the attachment limitation after expansion, the size for making it not washed away stripping by flowing water, matrix is macromolecular material, polymer composite, Inorganic Non-metallic Materials, the compound of inorganic non-metal composite material or macromolecular material and Inorganic Non-metallic Materials, attachment is polymer substance.Water-treatment biological membrane reactor of the invention can effectively purify waste water, and with being not easily blocked, small energy consumption and the characteristics of low cost, with extraordinary Industry Promotion advantage.
Description
Technical field
The invention belongs to sewage treatment area, it is related to a kind of water-treatment biological membrane reactor.
Background technology
In recent years, as China's economy is developed rapidly, the sustainable growth of simultaneous population, a large amount of pollutants are discharged into
In the earth's surface aquatic ecosystem such as rivers and lakes, river basin ecological environment is caused to be destroyed, it is serious to restrict the sustainable of economic society
Development, influences the quality of life of people.The continuing to develop to be had become with engineer applied of sewage disposal technology maintains social economy
The necessary component of sustainable development.Various sewage treatment process based on physics, chemistry and biology principle continuously emerge,
Wherein biologic treating technique is most widely used, and has become the prevailing technology of municipal sewage and organic industrial sewage treatment.
There is economic, effective, environment-friendly, non-secondary pollution due to biological prosthetic, and the money of pollution can be realized
Sourceization is utilized, and is reliable method.In biological renovation method, algae, aquatic animal and water plant, or based on aquatic
Though the artificial swamp or land system of plant have certain effect, its efficiency is low, it is poor to take up an area many, repairing effect.And use micro-
Biological method treatment, effect is good, efficiency high, especially biomembrance process therein to the removal efficiency of the Organic substance in water etc. that gives up compared with
Height, has been widely used in the processing procedure of water and waste water.With the breakthrough of supporting technology and material, in recent years
Biomembrane process has obtained the very big concern of numerous researchers and engineers and technicians, and development is quite rapid, to biomembrane feature
Understanding and fundamental research constantly deepen, existing actual process becomes better and approaching perfection day by day, while occurring in that the biology of various new
Membrane reactor technique and various group technologies, have gradually formed a set of more complete biomembrance process biologic process for treating sewage system
Row.
The type of known existing biofilms reactor has with technology:Ordinary biofilter (aerobic), high-loading logical filter
(aerobic), tower biological filter (aerobic), anaerobic biofilter (anaerobism), activated biofiler (aerobic), aerobe rotating disk
(aerobic), anaerobic organism rotating disk (anaerobism), submerged bacteria filter (aerobic), micro-pore film biological reaction device (aerobic), biological stream
Change bed (aerobic), gas stripping type biofilm reactor (aerobic), mechanical agitation bed (aerobic, anaerobism), anaerobic organism film expanded bed (to detest
Oxygen), MBBR (aerobic, anaerobism), complex biofilmreactor, activated sludge-biofilm reactor, sequence
Batch biofilm reactor, upflow anaerobic sludge blanket process-anaerobic biofilter, apposition growth Wastewater Stabilization Ponds, these technologies are all
In being widely used in engineering because of each exclusive characteristic.
The A of Chinese patent CN 105174436 disclose a kind of biofilm aeration reactor, and it passes through to add 2 groups of microorganisms
Filler makes water process reach a new standard, and two kinds of microbe stuffings can select aerobic microbiological, also may be selected one
It is anaerobe to plant as aerobic microbiological is another, and using 2 groups of microbiological treatment water bodys, COD is significantly lower than a kind of microorganism
The sewage for the treatment of, meanwhile, reactor is still as good as with traditional size, and treatment is substantially increased while floor space is not expanded
Effect.
The B of Chinese patent CN 102015551 provide a kind of biofilm reactor containing helical structure, biomembrane reaction
Device has helical structure wherein, for forming the spiral froth flow passage from air supply pipe to outlet so that pass through
The foam for causing air supply pipe to be supplied flows and improves oxygen transfer rate by increasing the residence time of foam.The biomembrane
The advantage of reactor is that microorganism is attached to the helical structure and biomembrane is formed on the helical structure, so that real
Microbial suspension growth and two kinds of conditions of attached growth of microorganisms, and the energy under conditions of not using energy to be stirred are showed
The concentration of oxygen in water is enough effectively improved, and can effectively improve and keep the concentration of microorganism.
The A of Chinese patent CN 102951735 disclose a kind of combined type baffling water-treatment biological membrane reactor, with water inlet
Mouth, delivery port and drain, its feature exist:In a pond body for rectangle, by influent stream dividing plate, going out to flow dividing plate, advection plate will be anti-
Device is answered to be separated into relatively independent anoxic zone, aerobic zone and advection area.The invention aerobic zone and anoxic distinguish independent control, can
Reduction is interfered, and more preferably, technique is easy to operation to treatment effect, may be used on the even industry of eutrophication water, breeding water body
Waste water it is biological prosthetic.
Specifically, biofilm reactor has the advantages that following aspects:
1) microbial variation, biological food chain length, and the microorganism that the generation time that can survive is more long;
2) microbial biomass is more, and disposal ability is big, and purification function is significantly improved;
3) sludge settling property is good, it is easy to which separation of solid and liquid, excess sludge production is few, reduces Treatment of Sludge and takes with disposal
With;
4) anti impulsion load, changes with stronger adaptability, and can process the sewage of low concentration to water quality, water;
5) it is easy to operational management, reduces sludge bulking problem.
But existing biofilm reactor there is also deficiency:The water process of the biomembrane composition on filler and its surface is constructed
Thing is easily blocked;Carrying out stilling need to be aerated in reactor when aerobic bacteria is processed, energy consumption is big;Aerobic, anaerobic bacteria typically can not be simultaneously
Depositing need to separate treatment etc..
Therefore, study it is a kind of can effectively purify waste water and do not block, energy consumption is small, low cost water-treatment biological membrane reactor
Have important practical significance.
The content of the invention
The present invention in view of the shortcomings of the prior art, there is provided one kind can effectively purify waste water and do not block, energy consumption is small, cost
Low water-treatment biological membrane reactor.
In order to achieve the above object, the technical solution adopted by the present invention is:
A kind of water-treatment biological membrane reactor, is mainly made up of matrix with the attachment for sticking to matrix surface, matrix
Attachment content is 0.15~0.5g/m in per surface2, matrix is plane mesh structure, after the attachment water suction of matrix surface
Expand the filling of matrix mesh is formed into water completely can not the film that can diffuse through of directly penetrating but Organic substance in water, matrix mesh
Size be less than or equal to critical dimension, the critical dimension be mesh just by after expansion attachment limitation, it is not flowed
Water washes away the size of stripping.
As preferred technical scheme:
A kind of water-treatment biological membrane reactor as described above, the attachment is adhered directly to matrix surface or passes through
Binder sticks to matrix surface.
A kind of water-treatment biological membrane reactor as described above, described matrix be macromolecular material, polymer composite,
The compound of Inorganic Non-metallic Materials, inorganic non-metal composite material or macromolecular material and Inorganic Non-metallic Materials.
A kind of water-treatment biological membrane reactor as described above, the thickness of described matrix is 0.1~5mm, preferably 0.5~
2mm, the aperture of described matrix mesh is 10~1000 mesh, preferably 50~500 mesh, the Unit Weight of described matrix for 10~
1000g/m2, preferably 100~500g/m2。
A kind of water-treatment biological membrane reactor as described above, tearing strength >=20N that described matrix goes up in any direction,
The anti-hydrolytic performance of described matrix is excellent, and under the natural conditions contacted with water, the term of tearing strength one of its any direction protects
Holdup is no less than 60%, and two term conservation rates are no less than 30%.
A kind of water-treatment biological membrane reactor as described above, the attachment is polymer substance, the polymer
Matter is cubical expansivity after saturation water suction>The mixture of 1000% resin, biogum or both, the resin is polyacrylic acid
Salt or polyacrylamide, the biogum are agar, xanthans or sodium alginate, when the polymer substance is mixture, tree
Fat is 0.5~9.5 with the mass ratio of biogum:9.5~0.5.
A kind of water-treatment biological membrane reactor as described above, also contains voluminous powder, voluminous powder in the attachment
With suction-operated, it can be enriched with the nutriment in absorption effluent, be decomposed for bacterium, the content of the voluminous powder is
The 0.1~10% of attachment quality.
A kind of water-treatment biological membrane reactor as described above, the voluminous powder is particle diameter≤50 μm and porosity of=
50% inertia powder, the excessive impulsive force being subject to of the particle diameter of inertia powder is larger easily to be washed away by current, the too small surface of particle diameter
Can larger, itself easy reunion, it is not easy to realize dispersed, the porosity of inertia powder is too small cannot to play good absorption
Effect, the inertia powder refers to the powder that will not dissolve, decompose or discharge the chemical substance for hindering bacterial growth in water.
A kind of water-treatment biological membrane reactor as described above, the inertia powder is diatomite or activated carbon.Beneficial effect
Really:
(1) a kind of water-treatment biological membrane reactor of the invention can effectively remove the organic matter in waste water, purify waste water, tool
There is the good value of environmental protection;
(2) a kind of water-treatment biological membrane reactor of the invention, accessing pending water flows through rather than passes through from reactor surface, dirty
The problem blocked in the absence of current in water treatment procedure, sewage treating efficiency is high;
(3) a kind of water-treatment biological membrane reactor of the invention can carry out Anaerobic Treatment and aerobic place to water simultaneously
Reason, without aeration, energy consumption is small, low cost, with extraordinary Industry Promotion advantage.
Brief description of the drawings
Fig. 1 is water-treatment biological membrane reactor schematic diagram.
Specific embodiment
The invention will be further elucidated with reference to specific embodiments.It should be understood that these embodiments are merely to illustrate this hair
Bright rather than limitation the scope of the present invention.In addition, it is to be understood that after the content for having read instruction of the present invention, art technology
Personnel can make various changes or modifications to the present invention, and these equivalent form of values equally fall within the application appended claims and limited
Fixed scope.
Embodiment 1
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly by matrix and the attachment for being adhered directly to matrix surface
Thing is constituted, and matrix is plane mesh structure, and the material of matrix is PET, and the thickness of matrix is 0.1mm, and the aperture of matrix mesh is
10 mesh, the Unit Weight of matrix is 10g/m2, the tearing strength that matrix is gone up in any direction is 20N, the anti-hydrolytic performance of matrix
Excellent, under the natural conditions contacted with water, one term of the tearing strength conservation rate of its any direction is 60%, and two terms kept
Rate is 30%, and attachment is the Sodium Polyacrylate that cubical expansivity is 8000% after absorbing water, and the molecular weight of Sodium Polyacrylate is 10
Ten thousand, attachment is evenly distributed on the surface of matrix, and attachment content is 0.15g/m in the per surface of matrix2。
Embodiment 2
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly sticking to matrix surface by matrix and by binder
Attachment composition, matrix is plane mesh structure, and the material of matrix is PET/PP compounds (mass ratio 1:1), the thickness of matrix
It is 5mm to spend, and the aperture of matrix mesh is 1000 mesh, and the Unit Weight of matrix is 1000g/m2, what matrix was gone up in any direction tears
Resistance to spalling is 80N, and the anti-hydrolytic performance of matrix is excellent, under the natural conditions contacted with water, the tearing strength of its any direction
One term conservation rate is 85%, and two term conservation rates are 60%, and attachment is the polymer substance for including voluminous powder, porous
The content of powder is the 10% of attachment quality, and polymer substance is the polypropylene that cubical expansivity is 7000% after saturation absorbs water
Acid amides, the molecular weight of polyacrylamide is 1,000,000, voluminous powder for particle diameter be 50 μm and porosity be 50% activated carbon, it is attached
The surface that thing is evenly distributed on matrix, attachment content is 0.2g/m in the per surface of matrix2。
Embodiment 3
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly by matrix and the attachment for being adhered directly to matrix surface
Thing is constituted, and matrix is plane mesh structure, and the material of matrix is glass, and the thickness of matrix is 0.5mm, and the aperture of matrix mesh is
50 mesh, the Unit Weight of matrix is 50g/m2, the tearing strength that matrix is gone up in any direction is 50N, the anti-hydrolytic performance of matrix
Excellent, under the natural conditions contacted with water, one term of the tearing strength conservation rate of its any direction is 75%, and two terms kept
Rate is 36%, and attachment is the polymer substance for including voluminous powder, and the content of voluminous powder is the 5% of attachment quality,
Polymer substance is the agar that cubical expansivity is 1100% after saturation absorbs water, and the molecular weight of agar is 10,000, and voluminous powder is grain
Footpath be 10 μm and porosity be 85% diatomite, attachment is evenly distributed on the surface of matrix, attached in the per surface of matrix
Thing content for 0.1g/m2。
Embodiment 4
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly by matrix and the attachment for being adhered directly to matrix surface
Thing is constituted, and matrix is plane mesh structure, and the material of matrix is glass/carbon fibre compound (mass ratio 2:1), the thickness of matrix is
1.5mm, the aperture of matrix mesh is 100 mesh, and the Unit Weight of matrix is 110g/m2, the tear that matrix is gone up in any direction is strong
It is 25N to spend, and the anti-hydrolytic performance of matrix is excellent, under the natural conditions contacted with water, the tearing strength of its any direction 1 year
Phase conservation rate is 78%, and two term conservation rates are 57%, and attachment is the polymer substance for including voluminous powder, voluminous powder
Content for attachment quality 1%, polymer substance be saturation water suction after cubical expansivity be 2000% xanthans, xanthan
The molecular weight of glue is 5,000,000, voluminous powder for particle diameter be 20 μm and porosity be 82% diatomite, attachment is evenly distributed on
The surface of matrix, attachment content is 0.32g/m in the per surface of matrix2。
Embodiment 5
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly sticking to matrix surface by matrix and by binder
Attachment composition, matrix is plane mesh structure, and the material of matrix is cotton, and the thickness of matrix is 2mm, the aperture of matrix mesh
It is 150 mesh, the Unit Weight of matrix is 200g/m2, the tearing strength that matrix is gone up in any direction is 30N, the hydrolysis of matrix
Function admirable, under the natural conditions contacted with water, one term of the tearing strength conservation rate of its any direction is 76%, two terms
Conservation rate is 55%, and attachment is the polymer substance for including voluminous powder, and the content of voluminous powder is attachment quality
2%, polymer substance is the sodium alginate that cubical expansivity is 3000% after saturation absorbs water, and the molecular weight of sodium alginate is 20
Ten thousand, voluminous powder for particle diameter be 28 μm and porosity be 86% diatomite, attachment is evenly distributed on the surface of matrix, matrix
Per surface on attachment content be 0.4g/m2。
Embodiment 6
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly sticking to matrix surface by matrix and by binder
Attachment composition, matrix is plane mesh structure, and the material of matrix is PET and the compound (mass ratio 2 of glass:3), matrix
Thickness be 2.5mm, the aperture of matrix mesh is 250 mesh, and the Unit Weight of matrix is 220g/m2, matrix goes up in any direction
Tearing strength be 35N, the anti-hydrolytic performance of matrix is excellent, under the natural conditions contacted with water, the tear of its any direction
One term of intensity conservation rate is 75%, and two term conservation rates are 50%, and attachment is the polymer substance for including voluminous powder,
The content of voluminous powder is the 0.1% of attachment quality, and polymer substance is that cubical expansivity is 3600% after saturation absorbs water
(mass ratio is 0.5 to the mixture of polyacrylate and agar:9.5), the molecular weight of Sodium Polyacrylate is 150,000, the molecule of agar
It is 1.2 ten thousand to measure, voluminous powder for particle diameter be 38 μm and porosity be 65% activated carbon, attachment is evenly distributed on the table of matrix
Face, attachment content is 0.35g/m in the per surface of matrix2。
Embodiment 7
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly by matrix and the attachment for being adhered directly to matrix surface
Thing is constituted, and matrix is plane mesh structure, and matrix is the PP compound (mass ratio 4 fine with carbon:3), the thickness of matrix is 3mm,
The aperture of matrix mesh is 400 mesh, and the Unit Weight of matrix is 420g/m2, the tearing strength that matrix is gone up in any direction is
45N, the anti-hydrolytic performance of matrix is excellent, and under the natural conditions contacted with water, the term of tearing strength one of its any direction protects
Holdup is 70%, and two term conservation rates are 47%, attachment is the polymer substance for including voluminous powder, and voluminous powder contains
It is the 4% of attachment quality to measure, and polymer substance is the polyacrylate and fine jade that cubical expansivity is 4500% after saturation absorbs water
(mass ratio is 9.5 to the mixture of fat:0.5), the molecular weight of Sodium Polyacrylate is 110,000, and the molecular weight of agar is 1.5 ten thousand, porous
Powder for particle diameter be 40 μm and porosity be 62% activated carbon, attachment is evenly distributed on the surface of matrix, the unit of matrix
Attachment content is 0.4g/m on surface2。
Embodiment 8
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly sticking to matrix by matrix and by binder
The attachment composition on surface, matrix is plane mesh structure, and the material of matrix is glass, and the thickness of matrix is 3.5mm, matrix net
The aperture in hole is 450 mesh, and the Unit Weight of matrix is 500g/m2, the tearing strength that matrix is gone up in any direction is 42N, matrix
Anti-hydrolytic performance it is excellent, under the natural conditions contacted with water, one term of the tearing strength conservation rate of its any direction is
72%, two term conservation rates are 47%, and attachment is the polymer substance for including voluminous powder, and the content of voluminous powder is attached
The 6% of amount of substance, polymer substance is the polyacrylate and xanthans that cubical expansivity is 4000% after saturation absorbs water
(mass ratio is 5 to mixture:5), the molecular weight of Sodium Polyacrylate is 140,000, and the molecular weight of xanthans is 5,200,000, and voluminous powder is
Particle diameter be 32 μm and porosity be 61% activated carbon, attachment is evenly distributed on the surface of matrix, in the per surface of matrix
Attachment content is 0.5g/m2。
Embodiment 9
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly sticking to matrix surface by matrix and by binder
Attachment composition, matrix is plane mesh structure, and the material of matrix is PET and the compound (mass ratio 2 of cotton:1), matrix
Thickness is 4mm, and the aperture of matrix mesh is 550 mesh, and the Unit Weight of matrix is 600g/m2, what matrix was gone up in any direction tears
Resistance to spalling is 53N, and the anti-hydrolytic performance of matrix is excellent, under the natural conditions contacted with water, the tearing strength of its any direction
One term conservation rate is 68%, and two term conservation rates are 44%, and attachment is the polymer substance for including voluminous powder, porous
The content of powder is the 7% of attachment quality, and polymer substance is the polypropylene that cubical expansivity is 6500% after saturation absorbs water
(mass ratio is 3.5 to the mixture of sour sodium and sodium alginate:6.5), the molecular weight of Sodium Polyacrylate be 160,000, sodium alginate point
Son amount is 250,000, voluminous powder for particle diameter be 43 μm and porosity be 57% activated carbon, attachment is evenly distributed on matrix
Surface, attachment content is 0.15g/m in the per surface of matrix2。
Embodiment 10
A kind of water-treatment biological membrane reactor, as shown in figure 1, mainly by matrix and the attachment for being adhered directly to matrix surface
Thing is constituted, and matrix is plane mesh structure, and the material of matrix is nylon66 fiber, and the thickness of matrix is 4.5mm, the aperture of matrix mesh
It is 750 mesh, the Unit Weight of matrix is 800g/m2, the tearing strength that matrix is gone up in any direction is 76N, the hydrolysis of matrix
Function admirable, under the natural conditions contacted with water, one term of the tearing strength conservation rate of its any direction is 79%, two terms
Conservation rate is 45%, and attachment is the polymer substance for including voluminous powder, and the content of voluminous powder is attachment quality
8%, polymer substance is that cubical expansivity is 6300% polyacrylamide and the mixture (quality of xanthans after saturation absorbs water
Than being 7:3), the molecular weight of polyacrylamide is 1,050,000, and the molecular weight of xanthans is 5,050,000, and voluminous powder is that particle diameter is 48 μm
And porosity is 58% activated carbon, attachment is evenly distributed on the surface of matrix, attachment content in the per surface of matrix
It is 0.25g/m2。
Claims (9)
1. a kind of water-treatment biological membrane reactor, it is characterized in that:It is main to be made up of with the attachment for sticking to matrix surface matrix,
Matrix is plane mesh structure, and being expanded after the attachment water suction of matrix surface can not be direct by matrix mesh filling formation water completely
The film that penetrating but Organic substance in water can be diffused through, the size of matrix mesh is less than or equal to critical dimension, the critical dimension
It is that mesh just limits the attachment after expansion, the size for making it not washed away stripping by flowing water.
2. a kind of water-treatment biological membrane reactor according to claim 1, it is characterised in that the attachment is directly adhered to
Matrix surface is sticked in matrix surface or by binder.
3. a kind of water-treatment biological membrane reactor according to claim 1, it is characterised in that described matrix is macromolecule material
Material, polymer composite, Inorganic Non-metallic Materials, inorganic non-metal composite material or macromolecular material and inorganic non-metallic material
The compound of material.
4. a kind of water-treatment biological membrane reactor according to claim 1, it is characterised in that the thickness of described matrix is
0.1~5mm, the aperture of described matrix mesh is 10~1000 mesh, and the Unit Weight of described matrix is 10~1000g/m2。
5. a kind of water-treatment biological membrane reactor according to claim 1, it is characterised in that described matrix is in any direction
On tearing strength >=20N, the anti-hydrolytic performance of described matrix is excellent, under the natural conditions contacted with water, its any direction
One term of tearing strength conservation rate be no less than 60%, two term conservation rates be no less than 30%.
6. a kind of water-treatment biological membrane reactor according to claim 1, it is characterised in that the attachment is macromolecule
Material, the polymer substance is cubical expansivity after saturation water suction>The mixture of 1000% resin, biogum or both,
The resin is polyacrylate or polyacrylamide, and the biogum is agar, xanthans or sodium alginate, the macromolecule
When material is mixture, resin is 0.5~9.5 with the mass ratio of biogum:9.5~0.5.
7. a kind of water-treatment biological membrane reactor according to claim 6, it is characterised in that also contain in the attachment
Voluminous powder, the content of the voluminous powder is the 0.1~10% of attachment quality.
8. a kind of water-treatment biological membrane reactor according to claim 7, it is characterised in that the voluminous powder is particle diameter
≤ 50 μm and the inertia powder of porosity of=50%, the inertia powder refers to that will not dissolve, decompose or discharge obstruction in water
The powder of the chemical substance of bacterial growth.
9. a kind of water-treatment biological membrane reactor according to claim 8, it is characterised in that the inertia powder is diatom
Soil or activated carbon.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108535173A (en) * | 2018-03-30 | 2018-09-14 | 鞍钢股份有限公司 | Method for simulating bacterial biofilm on surface of steel material in water environment |
CN108956441A (en) * | 2018-09-04 | 2018-12-07 | 鞍钢股份有限公司 | Test method for simulating corrosion of sulfate reducing bacteria in marine environment |
CN116375301A (en) * | 2023-06-05 | 2023-07-04 | 山东国宏生物科技有限公司 | Soybean oil wastewater treatment method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1073207A (en) * | 1991-12-11 | 1993-06-16 | 中国科学院沈阳应用生态研究所 | Preparation of membrane bioreactor for producing beer and alcohol |
CN101693775A (en) * | 2009-10-21 | 2010-04-14 | 北京国电富通科技发展有限责任公司 | Fixed microbe rubber granule filler, preparation and application thereof |
CN106310957A (en) * | 2015-07-03 | 2017-01-11 | 天津工业大学 | Nanometer fiber-reinforced hydrogel filter membrane and preparation method thereof |
-
2017
- 2017-04-25 CN CN201710277670.1A patent/CN106904743A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1073207A (en) * | 1991-12-11 | 1993-06-16 | 中国科学院沈阳应用生态研究所 | Preparation of membrane bioreactor for producing beer and alcohol |
CN101693775A (en) * | 2009-10-21 | 2010-04-14 | 北京国电富通科技发展有限责任公司 | Fixed microbe rubber granule filler, preparation and application thereof |
CN106310957A (en) * | 2015-07-03 | 2017-01-11 | 天津工业大学 | Nanometer fiber-reinforced hydrogel filter membrane and preparation method thereof |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108535173A (en) * | 2018-03-30 | 2018-09-14 | 鞍钢股份有限公司 | Method for simulating bacterial biofilm on surface of steel material in water environment |
CN108956441A (en) * | 2018-09-04 | 2018-12-07 | 鞍钢股份有限公司 | Test method for simulating corrosion of sulfate reducing bacteria in marine environment |
CN116375301A (en) * | 2023-06-05 | 2023-07-04 | 山东国宏生物科技有限公司 | Soybean oil wastewater treatment method |
CN116375301B (en) * | 2023-06-05 | 2023-08-18 | 山东国宏生物科技有限公司 | Soybean oil wastewater treatment method |
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