CN1215702A - Two-phase anaerobic membrane-biologic system and process for treatment of waste water - Google Patents
Two-phase anaerobic membrane-biologic system and process for treatment of waste water Download PDFInfo
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- CN1215702A CN1215702A CN98120176A CN98120176A CN1215702A CN 1215702 A CN1215702 A CN 1215702A CN 98120176 A CN98120176 A CN 98120176A CN 98120176 A CN98120176 A CN 98120176A CN 1215702 A CN1215702 A CN 1215702A
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- 239000002351 wastewater Substances 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title abstract description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000012528 membrane Substances 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000002253 acid Substances 0.000 claims abstract description 11
- 238000000855 fermentation Methods 0.000 claims abstract description 6
- 230000004151 fermentation Effects 0.000 claims abstract description 6
- 230000002053 acidogenic effect Effects 0.000 claims description 36
- 238000000926 separation method Methods 0.000 claims description 21
- 238000004065 wastewater treatment Methods 0.000 claims description 8
- 238000003672 processing method Methods 0.000 claims description 4
- 239000012466 permeate Substances 0.000 claims description 3
- 230000000696 methanogenic effect Effects 0.000 claims description 2
- 239000000047 product Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract description 2
- 244000005700 microbiome Species 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 238000012545 processing Methods 0.000 description 7
- 239000007787 solid Substances 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 4
- 238000013461 design Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005842 biochemical reaction Methods 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 230000000593 degrading effect Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 238000009790 rate-determining step (RDS) Methods 0.000 description 2
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Separation Using Semi-Permeable Membranes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
A process for treating waste water with two-phase anaerobic membrane-biological system comprising two anaerobic bioreactors which are individually controlled to generate acid and methane respectively and a membrane separator between them, includes delivering the waste water into acid-generating reactor, fermenting for generating acid, flowing of the acidified water into membrane separator, returning the concentrated water intercepted by membrane back to acid-generating reactor, flowing of the water that passes through membrane into methane-generating reactor, fermentation for generating methane and discharging. Its advantages are high rate of organic substance removal and load capability, stable running and high recovery rate of energy.
Description
The invention belongs to technical field of waste water processing, particularly bio-reactor combines with membrane separation apparatus and is used for the technology of wastewater treatment.
1971, Ghosh and Pohland proposed a kind of diphasic anaerobic biosystem (Two-phase Anaerobic Biosystem is called for short the BS system) that is used for wastewater treatment.This system sets up the bio-reactor of two independent controls, respectively cultivation and fermentation bacterium and methanogen.By regulating and control two reactors operating parameter separately respectively, form microorganism the suitableeest environment separately, give full play to its activity, to improve the processing efficiency and the operation stability of system.The relevant BS systematic research that scholars such as Cohen carry out in the eighties shows that under the same conditions, the operation stability of BS system has greatly improved than a traditional phase anaerobic technique.But traditional BS system still has the following disadvantages:
1, being separated is the key that diphasic anaerobic technique is achieved.General TPAD technology all is to adopt the kinetic control method.A large amount of tests show that there is certain limitation in the kinetic control method: at first, be separated not exclusively, microorganism may be run off from reactor and be entered methane-producing reactor in the acidogenic reactor; Secondly, solid matter residence time in acidogenic reactor is short, and organism is decomposed not exclusively, influences subsequent disposal, and treatment effect is descended.
2, which kind of waste water to be applicable to employing TPAD technology about, viewpoint is unified as yet, generally believes that the diphasic anaerobic biological treatment is applicable to the easy acidifying solubility organic waste water of processing.This has limited the range of application of BS system.
Film-biosystem is also referred to as membrane bioreactor, is meant a new system with membrane separation technique and the mutual organic assembling formation of bio-reactor.This is the practical application of high-tech in water technology.
Being applied to the film-biosystem (comprising aerobic film-biosystem and anaerobism film-biosystem) of wastewater treatment at present, is to combine with film separation unit at traditional bio-reactor end basically, and accompanying drawing 1 is seen in its flow process signal.
As can be seen from the figure, biochemical reaction takes place after entering bio-reactor in former water, partial organic substances in the former water is assimilated by the microorganism in the bio-reactor (mud) or is converted into other organism, the mixed solution of mud and reacted former water is by being pumped into membrane separation apparatus, the trapped fluid of membrane separation apparatus is back to bio-reactor and continues to finish biochemical reaction, and the liquid that sees through of membrane separation apparatus is then discharged by system.
It is complete substantially that this flow process is applied to aerobic film-biosystem technology, is applied to anaerobism film-biosystem technology and then shows certain weak point, mainly comprise:
1, anaerobion is divided into fermenting bacteria and methanogen, two kinds of growing environment differences that microorganism is suitable,
Should not be placed in the reactor and grow.The branch mutually that is unfavorable for two kinds of microorganisms at the terminal blooming of reactor
From, thereby be unfavorable for bringing into play the advantage of various microorganisms.
2, solid matter all is trapped in the main body anaerobic reactor, influences the operation of reactor (the particularly UASB reactor of widespread use).
The objective of the invention is to, for overcoming the weak point of prior art, on the basis of above-mentioned technology, segments theory in conjunction with anaerobically fermenting, propose a kind of film separation unit and traditional diphasic anaerobic bio-reactor combination all-in-one-piece diphasic anaerobic film-biosystem and processing method thereof, make it have very high organic removal rate and very high load, and system is stable, the energy recovery rate advantages of higher.
A kind of diphasic anaerobic film-biosystem that is used for wastewater treatment comprises two independent product acid and methanogenic bio-reactors of controlling, and it is characterized in that, between two bio-reactors a membrane separation apparatus is set also.
Diphasic anaerobic film-the biosystem of the present invention's design is handled the processing method of waste water, may further comprise the steps:
1) pending waste water is sent to acidogenic reactor, and water outflow acidogenic reactor acidified in acidogenic reactor enters membrane separation apparatus;
2) said acidified water filters through membrane module in membrane separation apparatus, and the condensed water of being held back by membrane module is back to acidogenic reactor, and enters methane-producing reactor by the water of membrane module;
3) permeate water is discharged behind the gassy fermentation in methane-producing reactor;
4) biogas that is produced in acidogenic reactor and the methane-producing reactor is discharged behind water seal arrangement.
The present invention has following characteristics:
1, waste water diphasic anaerobic film-biosystem (Two-phase Anaerobic Membrane-Biosystem of the present invention's proposition, be called for short the MBS system) and sewage treatment technology process, being about to membrane separation technique combines with traditional diphasic anaerobic biosystem, and film separation unit placed between the two-phase reactor, the effect of its membrane module is: the acid-producing bacteria in the acidogenic reactor is held back back acidogenic reactor, make acidogenic reactor keep the acid-producing bacteria of high quantity; Membrane module cuts back acidogenic reactor with undecomposed suspended solid simultaneously, increase the solid retention time of these materials, enabled abundant hydrolysis and produce acid, strengthened the acid production of acidogenic reactor, make system reach higher acidification rate, and then improve the methanation rate of system; Hold back solid matter, guarantee that methane-producing reactor (UASB) has the water inlet that contains a large amount of low molecular weight volatile acid and do not contain SS, increases the operational efficiency of methane-producing reactor and stability; Finally reach the purpose that improves the organic pollutant removal rate and reclaim bioenergy.
2, film separation unit can be held back undecomposed macromolecule organic and suspended substance and anerobe and make it be back to acidogenic reactor, make organic substance residence time lengthening in acidogenic reactor, anerobe quantity increases, help its degradation of organic substances, so can carry out the processing of high organic loading, the kind of the waste water of processing from original BS system the basis of the easy degrading waste water of treatable solubility expand the easy degrading waste water that contains the high concentrated, solid suspended substance and the organic waste water of some difficult degradations to;
3, the crown_interception of the operation of acidogenic reactor and film will help the stability increase of system handles, make it anti impulsion load;
4, the adding of membrane module helps the biphase separation;
5, surplus sludge volume is few.
MBS of the present invention system is a kind of efficient, energy-conservation novel process system, and it is having higher utility and good prospects for application aspect the processing of high concentrated organic wastewater.
Brief Description Of Drawings;
Fig. 1 is that traditional film-biological effluent treatment system forms synoptic diagram.
Fig. 2 is embodiments of the invention system and processing technological flow figure.
Diphasic anaerobic film-the biosystem (MBS) and the technical process embodiment of a kind of wastewater treatment of the present invention's design as shown in Figure 2, in conjunction with the accompanying drawings, are described in detail as follows:
Diphasic anaerobic film-the biosystem (MBS) and the technical process embodiment of a kind of wastewater treatment of the present invention's design as shown in Figure 2, in conjunction with the accompanying drawings, are described in detail as follows:
Membrane module 9 places between acidogenic reactor 4 and the methane-producing reactor 11, and promptly system is by nucleus equipment: acidogenic reactor+membrane separation apparatus+methane-producing reactor is formed.Acidogenic reactor 4 places 35+0.5 ℃ of thermostat container 5 with methane-producing reactor 11, and waste water is stored in distributing trough 1.Waste water is delivered to acidogenic reactor 4 by pump 3, acidified water flows out from acidogenic reactor and enters film groove 10 and regulate pH value 6 in acidogenic reactor, in film groove 10 through the filtration of membrane module 9 (by film power-driven pump 15 suctions of membrane module), sent back to flow to through pump 8 and continue acidogenic fermentation in the acidogenic reactor by the condensed water (containing undecomposed macromolecule organic, suspended substance, microorganism etc.) that membrane separation apparatus is held back, carry out discharging 12 behind the gassy fermentation and permeate water (mainly containing volatile acid) is fed into methane-producing reactor by pump 15.The biogas that is produced in acidogenic reactor and methane-producing reactor emptying after entering gas meter 14 metering tolerance behind the water seal arrangement 13.Be provided with fluid level controller 7 in the film groove.
Membrane separation apparatus is the important component part of MBS system, and it places between acidogenic reactor and the methane-producing reactor, plays the effect of holding back larger molecular organics and suspended substance (comprising microorganism) and the matrix of being convenient to utilize being provided for microorganism in the methane-producing reactor.The present embodiment membrane separation apparatus is one group of External Pressure Type polypropylene hollow fiber membrane assembly.Film body is by Materials science institute of Zhejiang University or National Bureau of Oceanography's sea water desaltination manufacturing.Membrane module adopts the suction type periodical operation, establishes the film inlet flume, is submerged in below the trough inner water face during assembly running, and the methane-producing reactor air inlet influence methanogen and grows when preventing to aspirate.Because the film inlet flume can merge with the negative area at acidogenic reactor top, therefore the form that splits of this membrane module and acidogenic reactor also can be considered as the distortion of integral type film-biosystem.
Under the situation that SS is low and organism is easily degraded in water inlet, producing methane phase is the rate-limiting step of entire reaction, so when carrying out reactor design, methane-producing reactor should adopt long hydraulic detention time.For SS high waste water and used water difficult to degradate, it is generally acknowledged that it is the rate-limiting step of entire reaction that acid phase is produced in hydrolysis, therefore, the hydraulic detention time of acidogenic reactor generally should be longer, so that the abundant acidication of organism in the waste water.
In the present embodiment, waste water belongs to the high type of SS.Adopt total hrt HRT
1=12hr, wherein, acidogenic reactor HRT
a=4hr, methane-producing reactor HRT
m=8hr changes the system volume load by changing water inlet COD concentration.
Claims (2)
1, a kind of diphasic anaerobic film-biosystem that is used for wastewater treatment comprises two independent product acid and methanogenic anaerobic biological reactors of controlling, and it is characterized in that, between said two bio-reactors a membrane separation apparatus is set also.
2, adopt diphasic anaerobic film as claimed in claim 1-biosystem to handle the processing method of waste water, may further comprise the steps:
1) pending waste water is sent to acidogenic reactor, and acidified water flows out from acidogenic reactor and enters membrane separation apparatus in acidogenic reactor;
2) said acidified water filters through membrane module in membrane separation apparatus, and the condensed water of being held back by membrane module is back to acidogenic reactor, and enters methane-producing reactor by the water of membrane module;
3) permeate water is discharged behind the gassy fermentation in methane-producing reactor;
4) biogas that is produced in acidogenic reactor and the methane-producing reactor is discharged behind water seal arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98120176A CN1075472C (en) | 1998-10-23 | 1998-10-23 | Two-phase anaerobic membrane-biologic system and process for treatment of waste water |
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|---|---|---|---|
| CN98120176A CN1075472C (en) | 1998-10-23 | 1998-10-23 | Two-phase anaerobic membrane-biologic system and process for treatment of waste water |
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| CN1215702A true CN1215702A (en) | 1999-05-05 |
| CN1075472C CN1075472C (en) | 2001-11-28 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1294439C (en) * | 2002-11-14 | 2007-01-10 | 三星电子株式会社 | Planar lens and method for fabricating the same |
| CN105668780A (en) * | 2014-11-21 | 2016-06-15 | 中国寰球工程公司 | Acidification quick-recovery anaerobic reaction system |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101357804B (en) * | 2007-07-31 | 2010-05-19 | 沈阳大学 | Low concentration sewage anaerobic treatment process |
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1998
- 1998-10-23 CN CN98120176A patent/CN1075472C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1294439C (en) * | 2002-11-14 | 2007-01-10 | 三星电子株式会社 | Planar lens and method for fabricating the same |
| CN105668780A (en) * | 2014-11-21 | 2016-06-15 | 中国寰球工程公司 | Acidification quick-recovery anaerobic reaction system |
| CN105668780B (en) * | 2014-11-21 | 2018-10-16 | 中国寰球工程公司 | It is acidified fast quick-recovery anaerobic reaction system |
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| Publication number | Publication date |
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| CN1075472C (en) | 2001-11-28 |
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