CN205061696U - Fluctuation freight elevator system integrates - Google Patents
Fluctuation freight elevator system integrates Download PDFInfo
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- CN205061696U CN205061696U CN201520788989.7U CN201520788989U CN205061696U CN 205061696 U CN205061696 U CN 205061696U CN 201520788989 U CN201520788989 U CN 201520788989U CN 205061696 U CN205061696 U CN 205061696U
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Abstract
The utility model relates to a fluctuation freight elevator system integrates, it includes that shell and encapsulation in shell inside and the anaerobism workspace that connects gradually, good oxygen workspace and mud disengagement zone, set up overflow arrangement between anaerobism workspace and the good oxygen workspace and between good oxygen workspace and the mud disengagement zone, the inside of mud disengagement zone sets up a plurality of dull and stereotyped film elements, sets up the back flow between bottom and the anaerobism workspace, dull and stereotyped film element includes panel beating electrode subassembly, the peaceful plate framework of osmotic membrane, and preceding, the back two sides installation osmotic membrane of dull and stereotyped frame set up panel beating electrode subassembly between the osmotic membrane, panel beating electrode subassembly includes two plate electrodes of connecting different outputs of alternating current power supply and insulation each other respectively, and the plate electrode is integrated into one piece's sheet metal component, be provided with the product water export of the product water cavity between two osmotic membranes of intercommunication on the dull and stereotyped frame. The utility model discloses can realize activated sludge's efficient handling, have integrated formula structure, take up an area of the advantage little, that environmental suitability is good.
Description
Technical field
The utility model relates to technical field of biological sewage treatment, is specifically related to a kind of integrated biomembrane reaction system.
Background technology
Waste water aerobic biologic treating technique can be divided into biomembrance process and the large class of activated sludge process two.Though activated sludge process is comparatively ripe, also there is a lot of shortcoming and defect, as large in floor space, capital cost is high, simultaneously poor to the adaptability of water quality, water yield change.Biomembrance process can make up many deficiencies of activated sludge process: good operation stability, without the volume of sludge bulking, reactor high to the clearance of pollutent and the advantage such as floor space is little.But traditional biomembrance process also has its defect, as biological filter is subject to blocking, need periodically to shut down to carry out back flushing, reaction cannot be carried out continuously.
Industrially mainly be divided into physical cleaning and matting through being commonly used to clean the method for fouling membrane, matting is by making with medicament so that insoluble pollutant dissolution is flushed out membrane module.But matting not only increases the running cost of filtration process due to the use of medicament, and film is caused damage due to the use of acid or basic agent and pollutes.Physical cleaning mainly comprises the method such as the cleaning of low pressure high flow rate, isobaric flushing, back flushing, negative pressure cleaning, mechanical curettage, generally uses high speed back flushing and air-water backwashing technique in industry.But, above-mentioned two kinds of techniques all must in cleaning process stopper film filtration process, and need high pressure and higher than water production rate two to three times water for rinse, consume energy high, water consumption is large.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, a kind of integrated biomembrane reaction system using the flat membrane component of built-in panel beating dielectrophoresis electrode assemblie is proposed, realize effective process of active sludge, there is integrated type structure, take up an area advantage that is little, good environmental adaptability.
The utility model solves its technical problem and is achieved through the following technical solutions:
A kind of integrated biomembrane reaction system, it is characterized in that: it comprises shell and is encapsulated in described enclosure and the anaerobism workspace connected successively, aerobic workspace and mud disengaging zone, arranges overflow device between described anaerobism workspace and aerobic workspace and between aerobic workspace and mud disengaging zone; The inside of described mud disengaging zone arranges multiple flat membrane component, arranges return line between bottom and described anaerobism workspace;
Described flat membrane component comprises panel beating electrode assemblie, permeable membrane and plate frame, and permeable membrane is installed on the forward and backward two sides of plate frame, arranges panel beating electrode assemblie between described permeable membrane; Described panel beating electrode assemblie comprises two panels and connects the different output terminal of AC power respectively and the battery lead plate of mutually insulated, the sheet metal component that described battery lead plate is formed in one, comprises the electrode of many flat shape arrangements and connects one or one or more sideline of all described electrodes simultaneously; Battery lead plate interfolded described in two, makes the electrode of a battery lead plate be placed between two adjacent electrodes of another battery lead plate; Described plate frame is provided with the product water out of the product water cavity between connection two permeable membrane.
Described battery lead plate is comb-like electrode plate, and comprise many electrodes arranged in parallel, and connect a sideline of all described electrode one end simultaneously, the other end of described electrode is free end; The sideline of one battery lead plate is arranged in the free end side of another battery lead plate electrode.
Described battery lead plate is grid electrode plate, comprises many electrodes arranged in parallel, and connects the sideline at two ends of described electrode respectively.
Described battery lead plate is three-dimensional grid electrode plate, comprises many electrodes arranged in parallel, and connects two sidelines at two ends of described electrode respectively; The two ends bending of described electrode, dodges mutually when interfolded.
Described in two, battery lead plate outside all arranges insulation layer; Or a battery lead plate outer setting insulation layer, another battery lead plate is the bare electrode that corrosion resistant material is made.
Each described product water out is connected to a product water delivery pipe jointly.
Described overflow device is overflow weir.
Whipping appts and traverse baffle are set in anaerobism workspace.
In described anaerobism workspace, fixing filler is set, the aerobic filler of the drift that can suspend is set in described aerobic workspace.
Described aerobic filler is the biomembranous moving bed biological filler of surface attachment.
Advantage of the present utility model and beneficial effect are:
1, integrated biomembrane reaction system of the present utility model, adopts integrated type structure, has and takes up an area advantage that is little, good environmental adaptability.Between anaerobism workspace and aerobic workspace and between aerobic workspace and mud disengaging zone, overflow device is set, effectively can intercepts the loss of active sludge in reaction process.Filtering membrane in mud disengaging zone can well retain the active sludge suspended in scavenging solution, makes active sludge not need to reflux through second pond again, reduces second pond and takes up an area and construction cost.Between the bottom of mud disengaging zone and anaerobism workspace, return line is set, the active sludge that anaerobism workspace is lost in the course of the work can be supplemented, and the effect of dilute sewage can be played, reduce influent COD cr concentration to the impact of anaerobic zone, when CODcr load diminishes, the efficiency of process improves; Also make the active sludge being deposited to water distribution area again increase with current and get back to anaerobic zone, prevent the loss of active sludge.
2, integrated biomembrane reaction system of the present utility model, adopt the flat membrane component containing panel beating electrode assemblie, by applying alternating-current on panel beating electrode assemblie, thus unshapeliness electric field is produced near dielectrophoresis electrode and permeable membrane, the principle that the external phase dielectric depolarization ability utilizing solia particle and its to suspend is different, solia particle is pushed away electrode or is adsorbed on electrode by solia particle by dielectrophoresis force, reduce the fouling membrane and stifled film phenomenon even eliminating and occur in permeable membrane technique, continuously-running, aspirate without the need to intermittent type, do not need on-line cleaning, save energy consumption.And filtering membrane can well retain the active sludge suspended in scavenging solution, make active sludge not need to reflux through second pond again, reduce second pond and take up an area and construction cost.
3, integrated biomembrane reaction system of the present utility model, battery lead plate in the panel beating electrode assemblie that flat membrane component uses is one-body molded by punching press, it is shaped with the electrode of many flat shape arrangements, and connect one or one or more sideline of described electrode, interfolded between two panels battery lead plate, makes the spaced correspondence of the electrode of two panels battery lead plate to form electrode group; Battery lead plate is one-body molded by sheet metal process, and production cost is low, and comparatively cylindrical electrode reduces costs more than 70%; Any one position connects power supply and whole plate can be made to be powered, thus makes electrode and be connected wire and be integrated on a sheet metal component; According to the difference of panel beating selection quality and thickness, certain flexibility or rigidity can be possessed, rollable or open and flat use; When mounted because relative position between each electrode sets, the one can carrying out whole battery lead plate is installed, and can not cause the confusion of electrode array
4, integrated biomembrane reaction system of the present utility model, battery lead plate battery lead plate in the panel beating electrode assemblie that flat membrane component uses can be set to comb-like electrode plate, when two panels comb-like electrode plate staggered formation panel beating dielectrophoresis electrode structure, the electrode of the first comb-like electrode plate inserts between the electrode of the second comb-like electrode plate, form electrode group, can prevent two panels battery lead plate from contacting in sideline when superposing like this, produce and interfere, there is structure very simplify, easy to manufacture, advantage easy for installation.
5, integrated biomembrane reaction system of the present utility model, battery lead plate in the panel beating electrode assemblie that flat membrane component uses can be grid electrode plate, when two panels grid electrode plate interleaved stacks formation panel beating dielectrophoresis electrode structure, the two ends of electrode are all linked together by sideline, therefore position is relatively fixing when mounted for electrode, does not need the later stage to adjust; And, in order to avoid the sideline of grid electrode plate contacts, the sideline bending of two battery lead plates can be made to dodge, also insulating trip can be set between the sideline of two battery lead plates.
6, integrated biomembrane reaction system of the present utility model, battery lead plate in the panel beating electrode assemblie that flat membrane component uses can be three-dimensional grid electrode plate, when the overlapping formation panel beating dielectrophoresis electrode structure of the three-dimensional grid electrode plate of two panels, intersect in the middle part of the electrode of two panels battery lead plate, form electrode group; And bend due to the two ends of electrode, there is gap between the sideline of therefore two three-dimensional grid electrode plates, can mutually insulated automatically.
7, integrated biomembrane reaction system of the present utility model, installs fixing filler, can solidify the anaerobic activated sludge be attached on anaerobism filler, make it can not enter aerobic workspace with current in anaerobism workspace.
8, integrated biomembrane reaction system of the present utility model, arranges whipping appts in anaerobism workspace, is stirred former water is mixed rapidly by power; And traverse baffle is set occurs short flow phenomenon to prevent equipment to be in operation, increase mud contact area simultaneously, strengthen the sludge loading of anaerobism workspace.
9, integrated biomembrane reaction system of the present utility model, be the aerobic filler of the drift that can suspend in aerobic workspace, and strengthen periphery aeration effect with tubular type aerating apparatus, aerobic filler can carry out random movement with aeration in whole aerobic workspace inside.The moving bed biological filler of aerobic filler preferred surface attached biological film, along with oxygen is by microbial consumption, microorganism in microbial film can natural layering, what be namely attached to biofilm surface is nitrifying bacteria community, denitrifying bacteria and other peculiar bacterium are then attached to biomembranous internal layer, oxidation of coal, nitrification and denitrification process are carried out at the different sites of compound film respectively, to improve sludge loading and the processing efficiency of aerobic zone.
Accompanying drawing explanation
Fig. 1 is integrated biomembrane reaction system architecture schematic diagram of the present utility model;
Fig. 2 is the internal structure schematic diagram of flat membrane component of the present utility model;
Fig. 3 is the external structure schematic diagram of flat membrane component of the present utility model;
Fig. 4 is of the present utility model when two battery lead plate superpositions, wherein connects the electrode position distribution schematic diagram of different output terminal;
Fig. 5 is electric field of the present utility model and dielectrophoresis force vector isogram;
Fig. 6 is the electrode plate structure schematic diagram of embodiment one of the present utility model;
Fig. 7 is the panel beating electrode assemblie structural representation of embodiment one of the present utility model;
Fig. 8 is the electrode plate structure schematic diagram of embodiment two of the present utility model;
Fig. 9 is the electrode plate structure schematic diagram of embodiment three of the present utility model;
Figure 10 is the front view of the panel beating electrode assemblie of embodiment three of the present utility model;
Figure 11 is the upward view of the panel beating electrode assemblie of embodiment three of the present utility model;
Figure 12 is the vertical view of the panel beating electrode assemblie of embodiment three of the present utility model;
Figure 13 is the flat membrane component sectional view of embodiment three of the present utility model.
Description of reference numerals
1-anaerobism workspace, the aerobic workspace of 2-, 3-mud disengaging zone, 4-flat membrane component, 5-sewage input tube, 6-produces water delivery pipe, 7-return line, 8-traverse baffle, 9-shell, 10-panel beating electrode assemblie, 11-permeable membrane, 12-plate frame, 13-produces water cavity, 14-flow-guiding cloth, 15-produces water out, 16-power supply adapter, 17-first electrode, 18-second electrode, 19-comb-like electrode plate, the electrode of 20-comb-like electrode plate, the sideline of 21-comb-like electrode plate, 22-grid electrode plate, the electrode of 23-grid electrode plate, the sideline of 24-grid electrode plate, the three-dimensional grid electrode plate of 25-, the electrode of the three-dimensional grid electrode plate of 26-, the sideline of the three-dimensional grid electrode plate of 27-.
Embodiment
Below by specific embodiment, the utility model is described in further detail, and following examples are descriptive, is not determinate, can not limit protection domain of the present utility model with this.
As shown in Figure 1, integrated biomembrane reaction system of the present utility model comprises the anaerobism workspace 1, aerobic workspace 2 and mud disengaging zone 3, shell 9 that connect successively and encapsulates as a whole by anaerobism workspace 1, aerobic workspace 2 and mud disengaging zone 3.Between anaerobism workspace 1 and aerobic workspace 2 and between aerobic workspace 2 and mud disengaging zone 3, arrange overflow weir, arrange multiple flat membrane component 4 in mud disengaging zone 3, each flat membrane component 4 is connected in parallel in an AC power, forms dull and stereotyped membrane stack.Return line 7 is set between mud disengaging zone 3 and anaerobism workspace 1, makes to enter active sludge in mud disengaging zone 3 and organic nitration product and get back to anaerobism workspace 1 and complete circulation.Unnecessary mud can be discharged outside system with sludge pump.
Sewage enters in anaerobism workspace 1 by sewage input tube 5, after carrying out anti-nitration reaction denitrogenation with anaerobic bacterium, enters aerobic workspace 2 by overflow manner; In aerobic workspace 2, aerobic bacteria carries out nitration reaction to organism simultaneously, and absorbs dephosphorization.The sewage overflow carried out after denitrogenation dephosphorizing enters mud disengaging zone 3, is separated by flat membrane component 4 pairs of sewage, produces water and enters product water cavity by filtering membrane and outwards export by producing water delivery pipe 6.Meanwhile, the dense water mixing active sludge is stayed in mud disengaging zone 3 and is carried out precipitated and separated, and the active sludge being deposited in bottom returns anaerobism workspace 1 by return line 7, and the dense water on top is pumped out.
Fixing filler is installed in anaerobism workspace 1, the anaerobic activated sludge be attached on anaerobism filler can be solidified, make it can not enter aerobic workspace 2 with current.And whipping appts is set wherein, stirred by power and former water is mixed rapidly; And traverse baffle 8 is set occurs short flow phenomenon to prevent equipment to be in operation, increase mud contact area simultaneously, strengthen the sludge loading of anaerobism workspace 1.
Be the aerobic filler of the drift that can suspend in aerobic workspace 2, and strengthen periphery aeration effect with tubular type aerating apparatus, aerobic filler can carry out random movement with aeration in whole aerobic workspace 2 inside.The moving bed biological filler of aerobic filler preferred surface attached biological film, along with oxygen is by microbial consumption, microorganism in microbial film can natural layering, what be namely attached to biofilm surface is nitrifying bacteria community, denitrifying bacteria and other peculiar bacterium are then attached to biomembranous internal layer, oxidation of coal, nitrification and denitrification process are carried out at the different sites of compound film respectively, to improve sludge loading and the processing efficiency of aerobic zone.
In anaerobism workspace 1, carry out anti-nitration reaction by denitrifying bacteria, utilize the organism in sewage to make carbon source, by the NO in sewage
3-N and NO
2-N is reduced to N
2be released in air, reach the object of denitrogenation; In the active sludge simultaneously refluxed addicted to phosphorus bacterium under anaerobic state, discharge a small amount of phosphorus.
In aerobic workspace 2, organism is degraded by microbial biochemical and continues to decline, and nitrifier utilizes BOD in water
5as hydrogen donor (organic carbon source), organonitrogen ammonification is then nitrated, make NH
3-N concentration significantly declines; Along with the continuation of nitrifying process, NO in water body
3the concentration of-N constantly increases; Addicted to phosphorus bacterium under aerobic situation to phosphorus excess ingestion, the concentration of phosphorus is declined fast, reaches the object of dephosphorization.Bacterial metabolism produce active sludge along with the sewage after denitrogenation dephosphorizing, by the overflow of aerobic workspace 2 to mud disengaging zone 3.
As shown in Figure 2,3, flat membrane component 4 of the present utility model comprises panel beating electrode assemblie 10, permeable membrane 11, plate frame 12, the forward and backward two sides of plate frame 12 adopts compression molding fashion to install permeable membrane 11, for producing water cavity 13 between two permeable membranes 11, panel beating electrode assemblie 10 is arranged on and produces in water cavity 13.Outside two battery lead plates and between two permeable membranes, flow-guiding cloth 14 is set respectively; The side of plate frame 12 is provided with the product water out 15 being communicated with and producing water cavity 13.The product water out 15 of all flat membrane components 4 connects product water delivery pipe 6 jointly.Plate frame 12 is ABS material preferably, and plate frame 12 and the mounting structure of permeable membrane 11 are the Sandwich Plates structure of replaceable permeable membrane, and replaceable when permeable membrane 11 is damaged, structural element reuses.Plate frame 12 is provided with power supply adapter 16.
Embodiment 1 about panel beating electrode assemblie 10:
Panel beating electrode assemblie 10 comprises the battery lead plate of two panels mutually insulated, and battery lead plate is directly cut or stamping forming sheet metal component in thin metal blank, comprises the electrode of many flat shapes arrangements and connects one or one or more sideline of all electrodes simultaneously; Two battery lead plate interfolded, the electrode of a battery lead plate is made to be placed in space between two adjacent electrodes of another battery lead plate, the different output terminals that two battery lead plates connect AC power by the power supply adapter 16 that plate frame 12 is arranged form electrode group, produce non-well-balanced electric field around.Two battery lead plates can all insulate, also can one insulation another be bare electrode; When there being a battery lead plate to be bare electrode, this battery lead plate should be corrosion resistant material, or through corrosion-resistance treatment.Phase between two output terminals of AC power preferably 180 ° time, near dielectrophoresis electrode and permeable membrane, produce unshapeliness electric field; And due to the frequency of AC power input different, in unshapeliness electric field, produce positive dielectrophoresis effect or negative dielectrophoresis effect.
As shown in Figure 4, the first electrode 17 (coating black) in the first battery lead plate is arranged on the neutral gear between the second electrode 18 (coating white) of the second battery lead plate, and the first electrode 17 and the second electrode 18 are staggered, and forms electrode group; First sideline and the second sideline are connected the different output terminals of AC power respectively, and the first sideline can be identical with the shape in the second sideline, also can be different.
As shown in Figure 5, when two output terminal of AC power is connected in the first sideline and the second sideline respectively, form non-uniform electric field between the crest line that electrode is relative, figure produces dielectrophoresis force vector isopleth along the length direction of electrode in dielectrophoresis electrod-array.
As shown in Figure 6, the two panels battery lead plate of the present embodiment is comb-like electrode plate 19, this comb-like electrode plate 19 is made up of many electrodes 20 arranged in parallel and the common sideline 21 connecting this electrode 20 one end, and the other end of many electrodes 20 arranged in parallel is free end.Two panels comb-like electrode plate 19 interfolded, between left and right every correspondence between the electrode 20 of two panels comb-like electrode plate 19, forms electrode group.As shown in Figure 7, when the overlapping formation panel beating dielectrophoresis electrode structure of two panels battery lead plate, the electrode 20 of the first comb-like electrode plate inserts between the electrode of the second comb-like electrode plate, forms electrode group.Can preventing two panels battery lead plate from contacting in sideline 21 when superposing like this, producing and interfering.The outside surface of comb-like electrode plate 19 all can arrange insulation layer, also can one insulation another be bare electrode plate; When there being a comb-like electrode plate 19 for bare electrode plate, this comb-like electrode plate 19 should be corrosion resistant material, or through corrosion-resistance treatment.
Embodiment 2 about panel beating electrode assemblie 10:
As shown in Figure 8, be with the difference of embodiment 1, two panels battery lead plate is grid electrode plate 22, and this grid electrode plate is made up of two sidelines 24 at many electrodes 23 arranged in parallel and the two ends that connect this electrode.Two panels grid electrode plate interval stacks, and forms electrode group.Adopt insulating trip to carry out interval between the sideline 24 of two panels grid electrode plate 22 to stack.When the overlapping formation panel beating dielectrophoresis electrode structure of two panels grid electrode plate 22, between the sideline 24 of two grid electrode plates 22, described insulating trip is set, the sideline 24 of grid electrode plate 22 can be avoided to contact, all can be linked together by sideline 24 due to the two ends of electrode 23, therefore position is relatively fixing when mounted for electrode, does not need the later stage to adjust.
Embodiment 3:
As shown in Figure 9, be with the difference of embodiment 2, two panels battery lead plate is three-dimensional grid electrode plate 25, this three-dimensional grid electrode plate 25 is made up of two sidelines 27 at many electrodes 26 arranged in parallel and the two ends that connect this electrode, the two ends of electrode 26 after the bending of homonymy direction, then connect two sidelines respectively.Preferred mode is: the two ends of electrode 26 to perpendicular to after the direction bending of electrode, then to being parallel to the direction 90-degree bent of electrode 26, are formed stepped, make the middle part of electrode 26 protruding relative to two ends.As shown in Figure 10, Figure 11, the outer portions interval of the three-dimensional grid electrode plate 25 of two panels stacks, and interlacedly between the electrode 26 of the three-dimensional grid electrode plate 25 of two panels stacks, and forms electrode group.As shown in figure 12, because the two ends of electrode 26 bend, there is gap between the sideline 27 of therefore two three-dimensional grid electrode plates 25, can mutually dodge automatic insulation.As shown in figure 13, between the relative sideline of two battery lead plates, mounting block is set, two battery lead plates are fixed as one.
The working process that inside arranges the flat membrane component 4 of panel beating electrode assemblie 10 is:
Flat membrane component 4 involved by the utility model is soaked in be needed in waste water to be processed, and due to the dielectric depolarization ability lower relative to water, solid particulate is usually expressed as negative dielectrophoresis character in waste water; Namely, in unshapeliness electric field, solid particulate is moved by weak electric field direction.As shown in Figure 2 and Figure 3, waste water is through the surface of permeable membrane 11, and the panel beating electrode assemblie 10 in permeable membrane 11 provides the electric field of the unshapeliness needed for dielectrophoresis force.When in waste water, solid particulate is near permeable membrane 11, under the effect of dielectrophoresis force, solid particulate moves to the direction away from permeable membrane 11, and so reducing even elimination fouling membrane and stifled film must occur; Water purification enters the product water cavity 13 between two permeable membranes 11 by permeable membrane 11, then is discharged by the product water out 15 be communicated with product water cavity 13.
Although disclose embodiment of the present utility model and accompanying drawing for the purpose of illustration, but it will be appreciated by those skilled in the art that: in the spirit and scope not departing from the utility model and claims, various replacement, change and amendment are all possible, therefore, scope of the present utility model is not limited to the content disclosed in embodiment and accompanying drawing.
Claims (10)
1. an integrated biomembrane reaction system, it is characterized in that: it comprises shell and is encapsulated in described enclosure and the anaerobism workspace connected successively, aerobic workspace and mud disengaging zone, arranges overflow device between described anaerobism workspace and aerobic workspace and between aerobic workspace and mud disengaging zone; The inside of described mud disengaging zone arranges multiple flat membrane component, arranges return line between bottom and described anaerobism workspace;
Described flat membrane component comprises panel beating electrode assemblie, permeable membrane and plate frame, and permeable membrane is installed on the forward and backward two sides of plate frame, arranges panel beating electrode assemblie between described permeable membrane; Described panel beating electrode assemblie comprises two panels and connects the different output terminal of AC power respectively and the battery lead plate of mutually insulated, the sheet metal component that described battery lead plate is formed in one, comprises many electrodes arranged in parallel and connects one or one or more sideline of all described electrodes simultaneously; Battery lead plate interfolded described in two, makes the electrode of a battery lead plate be placed between two adjacent electrodes of another battery lead plate; Described plate frame is provided with the product water out of the product water cavity between connection two permeable membrane.
2. a kind of integrated biomembrane reaction system as claimed in claim 1, it is characterized in that: described battery lead plate is comb-like electrode plate, comprise many electrodes arranged in parallel, and connect a sideline of all described electrode one end simultaneously, the other end of described electrode is free end; The sideline of one battery lead plate is arranged in the free end side of another battery lead plate electrode.
3. a kind of integrated biomembrane reaction system as claimed in claim 1, is characterized in that: described battery lead plate is grid electrode plate, comprises many electrodes arranged in parallel, and connects the sideline at two ends of described electrode respectively.
4. a kind of integrated biomembrane reaction system as claimed in claim 1, is characterized in that: described battery lead plate is three-dimensional grid electrode plate, comprises many electrodes arranged in parallel, and connects two sidelines at two ends of described electrode respectively; The two ends bending of described electrode, dodges mutually when interfolded.
5. the integrated biomembrane reaction system of the one as described in one of Claims 1 to 4, is characterized in that: described in two, battery lead plate outside all arranges insulation layer; Or a battery lead plate outer setting insulation layer, another battery lead plate is the bare electrode that corrosion resistant material is made.
6. the integrated biomembrane reaction system of the one as described in one of Claims 1 to 4, is characterized in that: each described product water out is connected to a product water delivery pipe jointly.
7. the integrated biomembrane reaction system of the one as described in one of Claims 1 to 4, is characterized in that: described overflow device is overflow weir.
8. a kind of integrated biomembrane reaction system as claimed in claim 1, is characterized in that: arrange whipping appts and traverse baffle in anaerobism workspace.
9. the integrated biomembrane reaction system of the one as described in claim 1 or 8, is characterized in that: arrange fixing filler in described anaerobism workspace, arranges the aerobic filler of the drift that can suspend in described aerobic workspace.
10. a kind of integrated biomembrane reaction system as claimed in claim 9, is characterized in that: described aerobic filler is the biomembranous moving bed biological filler of surface attachment.
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| CN201520788989.7U CN205061696U (en) | 2015-10-13 | 2015-10-13 | Fluctuation freight elevator system integrates |
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|---|---|---|---|
| CN201520788989.7U CN205061696U (en) | 2015-10-13 | 2015-10-13 | Fluctuation freight elevator system integrates |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106565015A (en) * | 2015-10-13 | 2017-04-19 | 内蒙古天环境技术有限公司 | Integrated biofilm reaction system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106565015A (en) * | 2015-10-13 | 2017-04-19 | 内蒙古天环境技术有限公司 | Integrated biofilm reaction system |
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Granted publication date: 20160302 Termination date: 20211013 |