CN101733046A - Three-phase fluidized-bed reactor - Google Patents
Three-phase fluidized-bed reactor Download PDFInfo
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- CN101733046A CN101733046A CN200810234319A CN200810234319A CN101733046A CN 101733046 A CN101733046 A CN 101733046A CN 200810234319 A CN200810234319 A CN 200810234319A CN 200810234319 A CN200810234319 A CN 200810234319A CN 101733046 A CN101733046 A CN 101733046A
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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
- 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
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Abstract
The invention discloses a three-phase fluidized-bed reactor. The three-phase fluidized-bed reactor solves the technical problems of poor gas-water mixing, difficult operation, undesirable solid-liquid separating effect and high effluent turbidity of an internal circulating three-phase fluidized-bed reactor. The three-phase fluidized-bed reactor comprises a gas-water mixing area, a reacting area, separating area and a filtrating area; the gas-water mixing area is, through a micro-porous gas distributor, communicated with the reacting area which is formed by an outer barrel and an inner barrel; a precipitating area and the filtrating area are formed outside the separating area on the top and communicated with each other through a perforated plate; the filtrating area is provided with a filtering component; and the filtrating component is connected with a water outlet and back wash system which comprises a water pump, a plurality of valves, a plurality of flowmeters and the like. The three-phase fluidized-bed reactor is characterized in that: the gas-water mixing area is shaped as a column; and the filtering component is a film component. The three-phase fluidized-bed reactor is used for treating the domestic sewage and the industrial effluent, so the municipal sewage is recycled to meet the municipal non-drinking water quality standards.
Description
Technical field
The present invention relates to environmental protection and biochemical reaction equipment technical field, particularly a kind of three-phase fluidized-bed reactor that is used for sanitary sewage and Industrial Wastewater Treatment.
Background technology
Bioremediation has been the main stream approach of current sewage disposal, and this mainly is that operating cost is low, and is easy and simple to handle because the bioanalysis capital expenditure is economized.Microorganism by assimilation and dissimilation degradation of contaminant and realize self propagation, is removed the removal that can realize organic matter, nitrogen, phosphorus and other pollutants behind the organic matter in the sewage by Separation of Solid and Liquid in reactor.Three-phase fluid bed reactor is one of biochemical reactor the most commonly used.Compare with traditional handicraft, the three-phase fluid bed reactor treatment effeciency is higher, and operating cost is lower, and effluent quality is better.
Internal-circulation type three-phase fluidization bed process is apposition growth biology or treatment based on immobilized microorganisms technology, and the carrier that is added suspends in water and constantly flow to form the fluidisation attitude with current.The characteristic feature of inside circulation triphase fluidized bed technology is to adopt inside and outside double-barrel structure, realizes the mixing of gas, water, carrier and forms circulating fluidized by the lifting of air at inner core.But in traditional fluid bed, promote speed and descend and backflow phenomenon occurs, and gas, water mixes and also have certain short stream, channeling, cause actual effective reacting volume to reduce owing to the effect of gravity and resistance to water-flow can produce.In the recent period this problem has obtained preliminary solution, promptly establish in the three-phase fluid bed reactor bottom reducing mouth mix to strengthen gas, water (Cao Wenping. novel reducing type three phase fluidized bed, application for a patent for invention number: 200620134874.7, publication number: CN200977457Y).But this kind reactor bottom is a cone, during practical engineering application constructional difficulties and also be not easy to the maintenance.
Compare with general bioreactor, inside circulation triphase fluidized bed reactor has very high biomass, can be up to 10g/L～20g/L, and good mixing effect, the mass-transfer efficiency of oxygen and utilization rate are also higher, so its hydraulic detention time is shorter, takes up an area of and lack reduced investment.But too high microbial biomass has aggravated the difficulty of Separation of Solid and Liquid, and it is up to standard to cause delivery turbidity to be difficult to.Filtering type highly effective separation and inside circulation triphase fluidized bed reactor (Jia Limin. filtering type highly effective separation and inside circulation triphase fluidized bed reactor, application for a patent for invention number: 200510012015.0, publication number: appearance CN 1721342A) makes this problem obtain preliminary solution.But the suspension major part of water outlet is still at 15mg/L～20mg/L, and waste water recycling is the inevitable requirement of " recycling economy promotion law ", and this technology can not satisfy objective demand fully.In addition, because microorganism concn is higher in the reactor, filtering layer stops up easily, needs frequent backwash, brings many difficulties to practical operation.
Summary of the invention
The technical problem that the present invention mainly solves is: inside circulation triphase fluidized bed consersion unit air water mixed effect is poor, the equipment operating difficulties, and solid-liquid separation effect is poor, and treatment effect is undesirable, the delivery turbidity height.For addressing this problem, technical scheme of the present invention is: a kind of three-phase fluidized-bed reactor, and it comprises air water mixed zone, reaction zone, Disengagement zone, filtering area; The air water mixed zone places this equipment foot, and its side bottom is provided with water inlet and air inlet; Reaction zone is by urceolus and inner core (9
1) constitute; The air water mixed zone is connected with reaction zone by the micropore air distribution plate; The Disengagement zone is positioned at the top of this equipment, is provided with annular settling zone and filtering area outside the Disengagement zone, and both are connected by perforated plate; Filtering area middle part is provided with filter assemblies, filter assemblies with by water pump, valve (17
1), valve (17
2), valve (17
3), valve (17
4), flowmeter (16
1), flowmeter (16
2) be connected with backwashing system with the water outlet of clear water reserviors composition, it is characterized in that the air water mixed zone is a cylindricality, the filter assemblies that the filtering area middle part is provided with is a membrane module.
The outer wall of air water mixed zone is connected by the consersion unit housing with urceolus, forms the deformation gauge structure between air water mixed zone and the reaction zone, i.e. side-looking is a trapezium structure wide at the top and narrow at the bottom.The air water mixed zone is a cylindricality, and its ratio of height to diameter is 1: 1～2: 1, air water mixed zone and inner core (9
1) the area ratio is 1: 1～1: 5.
The reaction zone middle part is provided with urceolus and inner core (9
1) double-barrel structure that constitutes, inner/outer tube area ratio is 1: 1.5～1: 5, urceolus and inner core (9
1) ratio of height to diameter of reaction zone of the double-barrel structure that constitutes is 6～12, inner core (9
1) bottom be horn mouth.
The consersion unit top is provided with Disengagement zone, settling zone and filtering area, and the Disengagement zone is connected by the ring-type perforated plate with the settling zone, but but settling zone bottom is provided with the spoil disposal (water) mouthful of not only spoil disposal but also draining.The top, settling zone is a filtering area, and the filtering area middle part is provided with filter assemblies, and this filter assemblies adopts ceramic membrane or hollow-fibre membrane.
Beneficial effect of the present invention is:
1, air water good mixing effect, easy construction and also be easy to the maintenance
Because the three-phase fluidized-bed reactor bottom is provided with air water mixed zone, the employing micropore air distribution plate gas distribution of cylindricality, air, waste water are after mix rapidly air water mixed zone limited below the perforated plate, form very big air water pressure, drive filler or immobilized microorganism and promote rapidly, make that promoting power strengthens with mode of jet.Can effectively improve the air water mixing efficiency, avoid the air water mixed zone to produce the dead band, effectively improve the utilization ratio of oxygen.The air water mixed zone of cylindricality is adopted in consersion unit bottom, easy construction and be easy to maintenance during practical engineering application.
2, good effect of separating solid from liquid, effluent quality is good
Since three-phase fluidized-bed reactor make full use of inside circulation triphase fluidized bed consersion unit to the pollutant highly-efficient treatment in, the coupled film filtering technique carries out Separation of Solid and Liquid efficiently to the consersion unit water outlet, good effect of separating solid from liquid, delivery turbidity is low, can hold back microorganism, prevent the microorganism loss, further improve microorganism concn in the consersion unit, the enhancement microbiological treatment effect.Because reaction medium carries out membrane filtration to filtering area after Disengagement zone, twice separation in settling zone in the consersion unit, can effectively alleviate film pollutes, reduce energy consumption, reduce the backwash frequency, reduce operating cost, effluent quality is good, can reach urban sewage reutilization city miscellaneous water water standard (GB T18920-2002).
Three-phase fluidized-bed reactor of the present invention and prior art effect relatively see Table 1.
Table 1 three-phase fluidized-bed reactor of the present invention and prior art effect are relatively
Description of drawings
Fig. 1 is a three-phase fluidized-bed reactor structural representation of the present invention.Wherein: 1 water inlet, 2 air inlets, 3 air water mixed zones, 4 micropore air distribution plates, 5 consersion unit housings, 6 horn mouths, 7 reaction zones, 8 urceolus, 9
1Inner core, 9
2Inner core, 10 spoil disposals (water) mouth, 11 Disengagement zone, twelve punch plate, 13 settling zones, 14 filtering areas, 15 filter assemblies, 16
1Flowmeter, 16
2Flowmeter, 17
1Valve, 17
2Valve, 17
3Valve, 17
4Valve, 18 water pumps, 19 clear water reserviors.
Fig. 2 is three-phase fluidized-bed reactor operation schematic diagram of the present invention.
The specific embodiment
The present invention is described in detail below in conjunction with accompanying drawing and example.
Embodiment 1:
A kind of three-phase fluidized-bed reactor, it comprises air water mixed zone (3), reaction zone (7), Disengagement zone (11), filtering area (14); Air water mixed zone (3) places this equipment foot, and its side bottom is provided with water inlet (1) and air inlet (2); Reaction zone (7) is by urceolus (8) and inner core (9
1) constitute; Air water mixed zone (3) is connected with reaction zone (7) by micropore air distribution plate (4); Disengagement zone (11) is positioned at the top of this equipment, and Disengagement zone (11) are outer to be provided with annular settling zone (13) and filtering area (14), and both are connected by perforated plate (12); Filtering area (14) middle part is provided with filter assemblies (15), filter assemblies (15) with by water pump (18), valve (17
1), valve (17
2), valve (17
3), valve (17
4), flowmeter (16
1), flowmeter (16
2) be connected with backwashing system with the water outlet of clear water reserviors (19) composition, particularly air water mixed zone (3) are cylindricality, the filter assemblies (15) that filtering area (14) middle part is provided with is a membrane module.
The outer wall of air water mixed zone (3) is connected by consersion unit housing (5) with urceolus (8), forms the deformation gauge structure between air water mixed zone (3) and the reaction zone (7), i.e. side-looking is a trapezium structure wide at the top and narrow at the bottom.Air water mixed zone (3) is a cylindricality, and the ratio of height to diameter of air water mixed zone (3) is 1: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 1.
Reaction zone (7) middle part is provided with urceolus (8) and inner core (9
1) double-barrel structure that constitutes, inner/outer tube area ratio is 1: 1.5, urceolus (8) and inner core (9
1) ratio of height to diameter of reaction zone (7) of the double-barrel structure that constitutes is 6, inner core (9
1) bottom be horn mouth (6).
The consersion unit top is provided with Disengagement zone (11), settling zone (13) and filtering area (14), and Disengagement zone (11) are connected by ring-type perforated plate (12) with settling zone (13), settling zone (13) but but the bottom is provided with the spoil disposal (water) mouthful (10) of not only spoil disposal but also draining.Top, settling zone (13) is filtering area (14), and filtering area (14) middle part is provided with filter assemblies (15), and this filter assemblies adopts ceramic membrane.
Its processing procedure is:
Adopt three-phase fluidized-bed reactor to handling through the coking chemical waste water of little electrolysis pretreatment and UASB Anaerobic Treatment, this waste water COD, SS are respectively about 900mg/, 300mg/L, pH=7.8.Coking chemical waste water and air enter air water mixed zone (3) by water inlet (1), air inlet (2) respectively, and air water mixes after micropore air distribution plate (4) enters reaction zone (7) with pattern rapidly in this limited space.In reaction zone (7), add the pollutant in the immobilized microorganism bead treatment of Coking Wastewater, described bead diameter 4～6mm, density 1.02g/cm
3, the reaction zone dissolved oxygen concentration is 6mg/L, waterpower is 30 ℃ with staying time 12h, temperature.At described consersion unit inner core (9
1) in, the immobilized microorganism bead mixes the back rapidly with gas-liquid two-phase and promotes.The coking chemical waste water and the immobilized microorganism bead that are thus lifted to the top flow downward at gravity effect lower edge consersion unit urceolus (8), and in Disengagement zone (11), the immobilized microorganism bead is from inner core (9
1) flow out the back by inner core (9
2) flow downward after stopping, thereby at inner core (9
1) and urceolus (8) formation circular flow.Liquid after the crude separation enters settling zone (13) through perforated plate (12), perforated plate (12) but effectively catching immobilized microorganism bead.Suspension in the settling zone (13) post precipitation discharge from spoil disposal (water) mouthful (10), the clear liquid up-flow after the separation is to filtering area (14), assembly (15) filters water outlet after the final Separation of Solid and Liquid after filtration, described filter assemblies (15) is a ceramic film component.After described three-phase fluidized-bed reactor moved through certain hour, stopping up can appear in fenestra, and filtration resistance increases, and filter efficiency descends.For guaranteeing the water outlet separating effect, membrane filtration system need carry out backwash.Valve (17 when normal operation
1), valve (17
2), valve (17
3) open valve (17
4) close, by flowmeter (16
2) the control water flow, by flowmeter (16
1) and valve (17
2) water circulation speed and guarantee filter assemblies (15) negative pressure in the controlled filter system.Valve (17 when backwash
1), valve (17
2), valve (17
4) open valve (17
3) close, by flowmeter (16
1) and valve (17
1) water circulation speed and guarantee that filter assemblies (15) malleation carries out backwash in the controlled filter system.Simultaneously, by spoil disposal (water) mouthful (10) draining.Reactor normally moves in backwash process, and backwash water is for being stored in the processing water outlet in the clear water reserviors (19).Described three-phase fluidized-bed reactor comprises complete automatic control system, is used for the automatic control and the adjustment of the reaction condition in the rate of circulating flow and fluid bed in the automatic backwash, fluid bed to membrane filtration system.Three-phase fluidized-bed reactor is system stable operation 30 days under these conditions, and treatment effect is stable.Water outlet COD is 60mg/L～90mg/L, and SS is≤5mg/L that water quality index reaches (GB8978-96) primary standard of country's " integrated wastewater discharge standard ".
Embodiment 2:
A kind of structure of three-phase fluidized-bed reactor and processing procedure are with embodiment 1.Wherein the ratio of height to diameter of air water mixed zone (3) cylindricality is 2: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 5, inner/outer tube area ratio is 1: 5, and the ratio of height to diameter of reaction zone (7) is for being 12, and filter assemblies adopts ceramic membrane, and its effect is with embodiment 1.
Embodiment 3:
A kind of structure of three-phase fluidized-bed reactor and processing procedure are with embodiment 1.Wherein the ratio of height to diameter of air water mixed zone (3) cylindricality is 1.5: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 3, inner/outer tube area ratio is 1: 3, and the ratio of height to diameter of reaction zone (7) is for being 8, and filter assemblies adopts ceramic membrane, and its effect is with embodiment 1.
Embodiment 4:
A kind of three-phase fluidized-bed reactor, it comprises air water mixed zone (3), reaction zone (7), Disengagement zone (11), filtering area (14); Air water mixed zone (3) places this equipment foot, and its side bottom is provided with water inlet (1) and air inlet (2); Reaction zone (7) is by urceolus (8) and inner core (9
1) constitute; Air water mixed zone (3) is connected with reaction zone (7) by micropore air distribution plate (4); Disengagement zone (11) is positioned at the top of this equipment, and Disengagement zone (11) are outer to be provided with annular settling zone (13) and filtering area (14), and both are connected by perforated plate (12); Filtering area (14) middle part is provided with filter assemblies (15), filter assemblies (15) with by water pump (18), valve (17
1), valve (17
2), valve (17
3), valve (17
4), flowmeter (16
1), flowmeter (16
2) be connected with backwashing system with the water outlet of clear water reserviors (19) composition, particularly air water mixed zone (3) are cylindricality, the filter assemblies (15) that filtering area (14) middle part is provided with is a membrane module.
The outer wall of air water mixed zone (3) is connected by consersion unit housing (5) with urceolus (8), forms the deformation gauge structure between air water mixed zone (3) and the reaction zone (7), i.e. side-looking is a trapezium structure wide at the top and narrow at the bottom.Air water mixed zone (3) is a cylindricality, and the ratio of height to diameter of air water mixed zone (3) is 1: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 1.
Reaction zone (7) middle part is provided with urceolus (8) and inner core (9
1) double-barrel structure that constitutes, inner/outer tube area ratio is 1: 1.5, urceolus (8) and inner core (9
1) ratio of height to diameter of reaction zone (7) of the double-barrel structure that constitutes is 6, inner core (9
1) bottom be horn mouth (6).
The consersion unit top is provided with Disengagement zone (11), settling zone (13) and filtering area (14), and Disengagement zone (11) are connected by ring-type perforated plate (12) with settling zone (13), settling zone (13) but but the bottom is provided with the spoil disposal (water) mouthful (10) of not only spoil disposal but also draining.Top, settling zone (13) is filtering area (14), and filtering area (14) middle part is provided with filter assemblies (15), and this filter assemblies adopts hollow-fibre membrane.
Its processing procedure is:
Three-phase fluidized-bed reactor of the present invention water inlet at first need pass through method removal larger particles impurity, floating thing and silts such as grid, heavy or flocculation just.Adopt three-phase fluidized-bed reactor that COD, SS are respectively about 300mg/L, 200mg/L, the sanitary sewage of pH=7.5 is handled.Sanitary sewage and air enter air water mixed zone (3) by water inlet (1), air inlet (2) respectively, and air water mixes after micropore air distribution plate (4) enters reaction zone (7) with pattern rapidly in this limited space.In reaction zone (7), add light filler and cultivate a large amount of microorganisms with the fluidized biomembrane form, the pollutant in the degraded sanitary sewage, described light filler is spherical porous polyethylene filler.The reaction zone dissolved oxygen concentration is 8mg/L, and waterpower is 30 ℃ with staying time 4h, temperature.At described consersion unit inner core (9
1) in, filler mixes the back rapidly with gas-liquid two-phase and promotes.The sanitary sewage and the filler that are thus lifted to the top flow downward at gravity effect lower edge consersion unit urceolus (8), and in Disengagement zone (11), the immobilized microorganism bead is from inner core (9
1) flow out the back by inner core (9
2) flow downward after stopping, thereby at inner core (9
1) and urceolus (8) formation circular flow.Liquid after the crude separation enters settling zone (13) through perforated plate (12), perforated plate (12) but the effectively catching filler.Suspension in the settling zone (13) post precipitation discharge from spoil disposal (water) mouthful (10), the clear liquid up-flow after the separation is to filtering area (14), assembly (15) filters water outlet after the final Separation of Solid and Liquid after filtration, described filter assemblies (15) material is a hollow fiber film assembly.After described three-phase fluidized-bed reactor moved through certain hour, stopping up can appear in fenestra, and filtration resistance increases, and filter efficiency descends.For guaranteeing the water outlet separating effect, membrane filtration system need carry out backwash.Valve (17 when normal operation
1), valve (17
2), valve (17
3) open valve (17
4) close, by flowmeter (16
2) the control water flow, by flowmeter (16
1) and valve (17
2) water circulation speed and guarantee filter assemblies (15) negative pressure in the controlled filter system.Valve (17 when backwash
1), valve (17
2), valve (17
4) open valve (17
3) close, by flowmeter (16
1) and valve (17
1) water circulation speed and guarantee that filter assemblies (15) malleation carries out backwash in the controlled filter system.Simultaneously, by spoil disposal (water) mouthful (10) draining.Reactor normally moves in backwash process, and backwash water is for being stored in the processing water outlet in the clear water reserviors (19).Described three-phase fluidized-bed reactor comprises complete automatic control system, is used for the automatic control and the adjustment of the reaction condition in the rate of circulating flow and fluid bed in the automatic backwash, fluid bed to membrane filtration system.Three-phase fluidized-bed reactor is system stable operation 30 days under these conditions, and treatment effect is stable.Water outlet COD is 10mg/L～30mg/L, and SS is≤5mg/L, and effluent quality reaches urban sewage reutilization city miscellaneous water water standard (GB T18920-2002).
Embodiment 5:
A kind of structure of three-phase fluidized-bed reactor and processing procedure are with embodiment 4.Wherein the ratio of height to diameter of air water mixed zone (3) cylindricality is 2: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 5, inner/outer tube area ratio is 1: 5, and the ratio of height to diameter of reaction zone (7) is for being 12, and filter assemblies adopts hollow-fibre membrane, and its effect is with embodiment 4.
Embodiment 6:
A kind of structure of three-phase fluidized-bed reactor and processing procedure are with embodiment 4.Wherein the ratio of height to diameter of air water mixed zone (3) cylindricality is 1.5: 1, air water mixed zone (3) and inner core (9
1) the area ratio is 1: 3, inner/outer tube area ratio is 1: 3, and the ratio of height to diameter of reaction zone (7) is for being 8, and filter assemblies adopts hollow-fibre membrane, and its effect is with embodiment 4.
Claims (4)
1. three-phase fluidized-bed reactor, it comprises air water mixed zone (3), reaction zone (7), Disengagement zone (11), filtering area (14); Air water mixed zone (3) places this equipment foot, and its side bottom is provided with water inlet (1) and air inlet (2); Reaction zone (7) is made of urceolus (8) and inner core (91); Air water mixed zone (3) is connected with reaction zone (7) by micropore air distribution plate (4); Disengagement zone (11) is positioned at the top of this equipment, and Disengagement zone (11) are outer to be provided with annular settling zone (13) and filtering area (14), and both are connected by perforated plate (12); Filtering area (14) middle part is provided with filter assemblies (15), filter assemblies (15) be connected with backwashing system by water pump (18), valve (171), valve (172), valve (173), valve (174), flowmeter (161), flowmeter (162) and the water outlet that clear water reserviors (19) are formed, it is characterized in that air water mixed zone (3) is cylindricality, the filter assemblies (15) that filtering area (14) middle part is provided with is a membrane module.
2. a kind of three-phase fluidized-bed reactor according to claim 1, the outer wall that it is characterized in that air water mixed zone (3) is connected by consersion unit housing (5) with urceolus (8), and formation variable-diameter structure, air water mixed zone (3) is a cylindricality, its ratio of height to diameter is 1: 1～2: 1, and air water mixed zone (3) are 1: 1～1: 5 with inner core (91) area ratio.
3. a kind of three-phase fluidized-bed reactor according to claim 1, it is characterized in that described reaction zone (7) middle part is provided with the double-barrel structure of urceolus (8) and inner core (91) formation, inner/outer tube area ratio is 1: 1.5～1: 5, urceolus (8) is 6～12 with the ratio of height to diameter of the reaction zone (7) of the double-barrel structure of inner core (91) formation, and inner core (91) bottom is horn mouth (6).
4. a kind of three-phase fluidized-bed reactor according to claim 1, it is characterized in that the consersion unit top is provided with Disengagement zone (11), settling zone (13) and filtering area (14), Disengagement zone (11) is connected by ring-type perforated plate (12) with settling zone (13), settling zone (13) but but the bottom is provided with the spoil disposal (water) mouthful (10) of not only spoil disposal but also draining.Top, settling zone (13) is filtering area (14), and filtering area (14) middle part is provided with filter assemblies (15), and this filter assemblies adopts ceramic membrane or hollow-fibre membrane.
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| CN200810234319A CN101733046A (en) | 2008-11-18 | 2008-11-18 | Three-phase fluidized-bed reactor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810234319A CN101733046A (en) | 2008-11-18 | 2008-11-18 | Three-phase fluidized-bed reactor |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102328989A (en) * | 2011-09-06 | 2012-01-25 | 浙江大学 | High-efficiency internal recycle ceramic-adhered biomembrane nitration reactor |
| CN102730638A (en) * | 2012-07-20 | 2012-10-17 | 神华集团有限责任公司 | Fluidized bed transformation reactor and fluidized bed transformation system with same |
| CN104045148A (en) * | 2014-07-09 | 2014-09-17 | 中国电建集团中南勘测设计研究院有限公司 | Inner-loop three-phase biological fluidized bed type membrane bioreactor (MBR) |
| CN106554075A (en) * | 2015-09-24 | 2017-04-05 | 北京联合创业环保工程股份有限公司 | Micro- aerobic recirculating fluidized bed membrane bioreactor and system |
| CN114314828A (en) * | 2021-12-31 | 2022-04-12 | 西南交通大学 | Anaerobic fluidized bed membrane bioreactor |
-
2008
- 2008-11-18 CN CN200810234319A patent/CN101733046A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102328989A (en) * | 2011-09-06 | 2012-01-25 | 浙江大学 | High-efficiency internal recycle ceramic-adhered biomembrane nitration reactor |
| CN102730638A (en) * | 2012-07-20 | 2012-10-17 | 神华集团有限责任公司 | Fluidized bed transformation reactor and fluidized bed transformation system with same |
| CN104045148A (en) * | 2014-07-09 | 2014-09-17 | 中国电建集团中南勘测设计研究院有限公司 | Inner-loop three-phase biological fluidized bed type membrane bioreactor (MBR) |
| CN104045148B (en) * | 2014-07-09 | 2016-02-17 | 中国电建集团中南勘测设计研究院有限公司 | A kind of inner loop three phase fluidized bed reactor formula MBR membrane bioreactor |
| CN106554075A (en) * | 2015-09-24 | 2017-04-05 | 北京联合创业环保工程股份有限公司 | Micro- aerobic recirculating fluidized bed membrane bioreactor and system |
| CN114314828A (en) * | 2021-12-31 | 2022-04-12 | 西南交通大学 | Anaerobic fluidized bed membrane bioreactor |
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