CN109867419A - A kind of new bio fluidized bed for Treatment of Coking Effluent - Google Patents
A kind of new bio fluidized bed for Treatment of Coking Effluent Download PDFInfo
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- CN109867419A CN109867419A CN201910305045.2A CN201910305045A CN109867419A CN 109867419 A CN109867419 A CN 109867419A CN 201910305045 A CN201910305045 A CN 201910305045A CN 109867419 A CN109867419 A CN 109867419A
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- main box
- component
- steel pipe
- lacing wire
- treatment
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- 238000004939 coking Methods 0.000 title claims abstract description 25
- 239000002351 wastewater Substances 0.000 claims abstract description 63
- 238000006243 chemical reaction Methods 0.000 claims abstract description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000001301 oxygen Substances 0.000 claims abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 17
- 238000012856 packing Methods 0.000 claims abstract description 17
- 230000000712 assembly Effects 0.000 claims abstract description 11
- 238000000429 assembly Methods 0.000 claims abstract description 11
- 238000005192 partition Methods 0.000 claims abstract description 11
- 238000005273 aeration Methods 0.000 claims abstract description 10
- 238000013019 agitation Methods 0.000 claims abstract description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 38
- 239000010959 steel Substances 0.000 claims description 38
- 239000007789 gas Substances 0.000 claims description 19
- 238000003756 stirring Methods 0.000 claims description 17
- 239000003365 glass fiber Substances 0.000 claims description 13
- 238000004064 recycling Methods 0.000 claims description 10
- 238000010992 reflux Methods 0.000 claims description 8
- 238000005276 aerator Methods 0.000 claims description 6
- 239000011152 fibreglass Substances 0.000 claims description 5
- 238000005243 fluidization Methods 0.000 abstract description 8
- 239000003245 coal Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 15
- 239000005416 organic matter Substances 0.000 description 12
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 10
- 238000001914 filtration Methods 0.000 description 6
- 244000005700 microbiome Species 0.000 description 6
- 230000000903 blocking effect Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000006065 biodegradation reaction Methods 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 230000000813 microbial effect Effects 0.000 description 3
- 238000006864 oxidative decomposition reaction Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 235000013555 soy sauce Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The invention discloses a kind of new bio fluidized beds for Treatment of Coking Effluent, belong to waste-water from coal mine processing applied technical field, including main box, water inlet component and outlet component, the main box is in rectangular configuration, water inlet component and outlet component are separately positioned on the two sides of main box, and both it is connected with the inside of main box, the top of main box is equipped with filter assemblies, the partition that its inner space can be divided into two impartial reaction chambers is equipped in main box, biologic packing material is filled in two reaction chambers, the air inlet being connected with a reaction chamber and two exhaust pipes are respectively equipped at the top of main box, aeration component is equipped in two reaction chambers, component is supplied oxygen equipped with the agitation that a reaction chamber adjacent thereto is connected in the water inlet component, whole design of the present invention is reasonable in design, coking wastewater can be carried out quick , efficient and stable fluidization treatment requirement, fluidisation operation safety stablizes.
Description
Technical field
The present invention relates to waste-waters from coal mine to handle applied technical field, more particularly, to a kind of for the new of Treatment of Coking Effluent
Type biological fluidized bed.
Background technique
Be discharged in industrial processes containing the waste water based on volatile phenol and non-volatile phenol.Coke-oven plant, gas generating station, conjunction
A large amount of phenol wastewater, Determination of Volatile Phenol in Refinery Wastewater and non-volatile phenol can be generated at production processes such as phenol factory, pharmaceutical factory, Fibre Plants
It often exists simultaneously, Coking Plant Wastewater mainly contains volatile phenol, and wastewater from gas generation plant mainly contains non-volatile phenol.Phenol wastewater, which removes, to be contained
Outside phenol, also containing pollutants such as oil, suspended matter, sulfide, ammonia nitrogen, cyanides.The color of coking of coal wastewater biochemical water outlet at present
For yellow or yellowish-brown, for coloration generally between 100-120-180 times, color is faint yellow or light yellow after processing, and is also wanted
Whether stable according to biochemistry, coloration is even up to 200 times or more into color of soy sauce.Common wastewater treatment adds in subsequent coagulation
Medicine can drop to 80 times of appearance, and the technique and system of color and operation using coloration after general decoloration medicament reaction precipitating
Operation quality it is closely related, coloration can't stably reaching standard it is exceeded so as to cause COD.General one substantially conforms to biochemical process
It is required that coking of coal comprehensive wastewater treating stations, remaining CODcr contamination data is discharged after stable operation mainly in original life
Change system is difficult the soluble contaminant substance of resolution, wherein just having the COD index of a large amount of coloration molecular contributions, to be postorder
It makes troubles coking waste water treatment process.
Therefore current, urgent need will design a kind of new bio fluidized bed for Treatment of Coking Effluent, realize useless to coking
Water carries out quick, efficient and stable fluidization treatment requirement.
Summary of the invention
The purpose of the present invention is to provide a kind of new bio fluidized beds for Treatment of Coking Effluent, to solve existing skill
Cannot achieve in art carries out the technical issues of quick, efficient and stable fluidization treatment requires to coking wastewater.
The present invention provides a kind of new bio fluidized bed for Treatment of Coking Effluent, including main box, water inlet component and
Outlet component, the main box is in rectangular configuration, and water inlet component and outlet component are separately positioned on the two sides of main box, and the two
It is connected with the inside of main box, the top of the main box is equipped with the filter assemblies being connected with inside it, in main box
Equipped with the partition that its inner space can be divided into two impartial reaction chambers, the upper end of the partition extends to filter assemblies
It is interior, it is filled with the biologic packing material with waste water phase reaction in two reaction chambers, is respectively equipped at the top of main box and is reacted with one
The air inlet and two exhaust pipes that chamber is connected, two reaction chambers are interior to be equipped with the aeration group being connected with two air inlets
Part, the interior agitation being connected to equipped with a reaction chamber adjacent thereto of the water inlet component supply oxygen component.
Further, the water inlet component includes left box body and four group of first lacing wire steel pipe, four group of first lacing wire steel pipe
Group is successively set in left box body from top to bottom, is located in the middle in one group of first lacing wire steel pipe and is fixed with the first glass reinforced plastic lattice
Screen, and every group of first lacing wire steel pipe includes several equidistant and in horizontally disposed first lacing wire steel pipe, left box body
Equipped with the water inlet pipe mouth and reflux water inlet being connected with inside it, left box body is fixedly connected with main box, and left box body leans on
The side wall of nearly main box is equipped with the first hole, is equipped with the first screen frame in first hole.
Further, the outlet component includes right case and four group of second lacing wire steel pipe, four group of second lacing wire steel pipe
Group is successively set in right case from top to bottom, and every group of second lacing wire steel pipe includes several equidistant and set in level
The the second lacing wire steel pipe set, right case are equipped with the effluent pipe mouth and recycling effluent mouth, right case and main tank being connected with inside it
Body is fixedly connected, and right case is equipped with the second hole close to the side wall of main box, is equipped with the second screen frame in second hole,
Recycling effluent mouth is connected with reflux water inlet by connecting pipe.
Further, the filter assemblies include the upper box being connected with two reaction chambers and are arranged at the top of main box
On the second glass fiber reinforced grid-like panel, the top of main box is equipped with two channel steels for fixing the second glass-fiber reinforced plastic grille board ends,
The upper section portion of partition is equipped with third hole.
Further, the aeration component includes main gas tube and several points of gas-guide tubes, the both ends of main gas tube respectively with
Two air inlets are connected, and several points of gas-guide tubes are symmetricly set in two reaction chambers and each divide gas-guide tube and main gas tube
It is connected, each divides gas-guide tube to be provided with several revolve and mix aerator.
Further, agitation oxygen supply component include the stirring air inlet being connected with the inside of left box body and with stirring
Two groups of air stirring pipes that air inlet is connected.
Further, one group of third lacing wire steel pipe being connected with the inner wall of main box is equipped in two reaction chambers
Group.
Compared with prior art, the beneficial effects of the present invention are:
By entering in left box body waste water from the water inlet pipe mouth on left box body, to stirring air inlet and two groups of air stirrings
It is passed through air in pipe, comes into full contact with air with waste water, has the function that aeration oxygen replenishing, improves postorder waste water and biologic packing material
Reaction effect is handled, waste water is filtered for the first time using the first glass fiber reinforced grid-like panel, plays the effect for blocking dirt, waste water is again from the
One hole is flowed into a reaction chamber adjacent thereto, wherein and the first screen frame in the first hole is for re-filtering to waste water,
Make suspended matter and fine particle in waste water etc. can not be as waste water enters in reaction chamber, by being passed through sky into two air inlets
Gas, and make air flowing into two reaction chambers in main gas tube and several points of gas-guide tubes, while several revolving mixed aerator
Work makes waste water obtain enough dissolved oxygens and waste water is driven to flow, and improves the organic matter and microorganism and dissolved oxygen in waste water
The effect of contact guarantees that the organic matter in waste water under conditions of having sufficient dissolved oxygen, carries out oxidative decomposition, secondly, will
Sundries, microorganism and dissolved oxygen in waste water etc. contact to form biomembrane with biologic packing material, increase microbial degradation organic contamination
The probability of object extends the residence time of organic matter, and the organic matter of biologic packing material adsorption is removed in enhanced biodegradation effect
It removes, the gas and sludge generated respectively in reaction can be discharged in sewage draining exit and two exhaust pipes, pass through the second glass reinforced plastic
Flase floor stops biologic packing material, and waste water enters another reaction chamber from third hole, realizes the secondary treatment work of waste water
Skill reaches the processing intent of high efficiency and high effect, using the second screen frame in the second hole to a reaction adjacent thereto
The biologic packing material of chamber carries out blocking filtering, and water after treatment is discharged from effluent pipe mouth, wherein using recycling effluent mouth, returns
Flowing into the mouth of a river and connecting pipe can be such that waste water handles by secondary cycle, and whole design of the present invention is reasonable in design, can be right
Coking wastewater carries out quick, efficient and stable fluidization treatment requirement, and fluidisation operation safety is stablized.
Detailed description of the invention
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art be briefly described, it should be apparent that, it is described below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is floor map one of the invention；
Fig. 2 is floor map two of the invention；
Fig. 3 is floor map three of the invention；
Appended drawing reference:
Main box 1, water inlet component 2, left box body 2a, the first lacing wire steel pipe 2b, the first glass fiber reinforced grid-like panel 2c, water inlet pipe
Mouth 2d, flow back water inlet 2e, the first screen frame 2f, outlet component 3, right case 3a, the second lacing wire steel pipe 3b, effluent pipe mouth 3c,
Recycling effluent mouth 3d, the second screen frame 3e, filter assemblies 4, upper box 4a, the second glass fiber reinforced grid-like panel 4b, channel steel 4c, third hole
4d, reaction chamber 5, partition 6, air inlet 7, exhaust pipe 8 are aerated component 9, and main gas tube 9a divides gas-guide tube 9b, revolve mixed aerator
9c stirs air inlet 10, air stirring pipe 11, third lacing wire steel pipe 12.
Specific embodiment
Technical solution of the present invention is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is a part of the embodiment of the present invention, instead of all the embodiments.
The component for the embodiment of the present invention for usually describing and showing in attached drawing here can be with a variety of different configurations
To arrange and design.Therefore, the detailed description of the embodiment of the present invention provided in the accompanying drawings is not intended to limit below and is wanted
The scope of the present invention of protection is sought, but is merely representative of selected embodiment of the invention.
Based on the embodiments of the present invention, those of ordinary skill in the art are obtained without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", "vertical",
The orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" be based on the orientation or positional relationship shown in the drawings, merely to
Convenient for description the present invention and simplify description, rather than the device or element of indication or suggestion meaning must have a particular orientation,
It is constructed and operated in a specific orientation, therefore is not considered as limiting the invention.In addition, term " first ", " second ",
" third " is used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can
To be mechanical connection, it is also possible to be electrically connected；It can be directly connected, can also can be indirectly connected through an intermediary
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood at this with concrete condition
Concrete meaning in invention.
Below with reference to shown in Fig. 1 to Fig. 3, the embodiment of the invention provides a kind of new bios for Treatment of Coking Effluent
Fluidized bed, including main box 1, water inlet component 2 and outlet component 3, the main box 1 is in rectangular configuration, water inlet component 2 and water outlet
Component 3 is separately positioned on the two sides of main box 1, and is both connected with the inside of main box 1, the top of the main box 1
Be equipped with equipped with the filter assemblies 4 being connected with inside it, in main box 1 its inner space can be divided into two it is impartial anti-
The partition 6 of chamber 5 is answered, the upper end of the partition 6 extends in filter assemblies 4, filled with opposite with waste water in two reaction chambers 5
The biologic packing material answered, the top of main box 1 are respectively equipped with the air inlet 7 being connected with a reaction chamber 5 and two exhaust pipes 8,
It is equipped with the aeration component 9 being connected with two air inlets 7 in two reaction chambers 5, is equipped with and its phase in the water inlet component 2
The agitation of an adjacent reaction chamber 5 connection supplies oxygen component.
The water inlet component 2 includes left box body 2a and four group of first lacing wire steel pipe 2b, four group of first lacing wire steel pipe 2b
It is successively set in left box body 2a from top to bottom, is located in the middle on one group of first lacing wire steel pipe 2b and is fixed with the first glass reinforced plastic
Flase floor 2c, and every group of first lacing wire steel pipe 2b includes several equidistant and is in horizontally disposed first lacing wire steel pipe,
The intensity of main box 1 is improved, left box body 2a is equipped with the water inlet pipe mouth 2d being connected with inside it and reflux water inlet 2e,
Left box body 2a is fixedly connected with main box 1, and left box body 2a is equipped with the first hole close to the side wall of main box 1, this first
The first screen frame 2f is equipped in hole, can be for re-filtering to waste water using the first screen frame 2f in the first hole, make waste water
In suspended matter and fine particle etc. can not enter in reaction chamber 5 with waste water.
The outlet component 3 includes right case 3a and four group of second lacing wire steel pipe 3b, four group of second lacing wire steel pipe 3b
It is successively set in right case 3a from top to bottom, and every group of second lacing wire steel pipe 3b includes several equidistant and in level
The second lacing wire steel pipe being arranged, improves the intensity of main box 1, and right case 3a is equipped with the outlet pipe being connected with inside it
Mouth 3c and recycling effluent mouth 3d, right case 3a is fixedly connected with main box 1, and right case 3a is on the side wall of main box 1
Equipped with the second hole, it is equipped with the second screen frame 3e in second hole, it can be in a reaction chamber 5 being located on the right of main box 1
Biologic packing material stopped, recycling effluent mouth 3d is connected with reflux water inlet 2e by connecting pipe, and recycling effluent is utilized
Mouth 3d, reflux water inlet 2e and connecting pipe can be such that waste water handles by secondary cycle, improve the treatment effect of coking wastewater.
The filter assemblies 4 include the upper box 4a being connected with two reaction chambers 5 and are arranged on 1 top of main box
Second glass fiber reinforced grid-like panel 4b, the top of main box 1 are equipped with two channel steels for fixing the second both ends glass fiber reinforced grid-like panel 4b
The upper section portion of 4c, partition 6 are equipped with third hole 4d, and the fixation by two channel steel 4c to the second glass fiber reinforced grid-like panel 4b prevents
When water flow passes through the second glass fiber reinforced grid-like panel 4b, drives the second glass fiber reinforced grid-like panel 4b to loosen, make the biology in a reaction chamber 5
Filler flows in another reaction chamber 5, can be made in a reaction chamber 5 on 1 left side of main box using third hole 4d
Waste water can flow in a reaction chamber 5 on the right of main box 1.
The aeration component 9 includes main gas tube 9a and several points of gas-guide tube 9b, and the both ends of main gas tube 9a are respectively with two
A air inlet 7 is connected, several points of gas-guide tube 9b be symmetricly set in two reaction chambers 5 and each divide gas-guide tube 9b with it is leading
Tracheae 9a is connected, and each divides gas-guide tube 9b to be provided with several revolve and mixes aerator 9c, by being passed through sky into two air inlets 7
Gas, and make air flowing into two reaction chambers 5 in main gas tube 9a and several points of gas-guide tube 9b, while several rotations are mixed exposes
Gas device 9c work makes waste water obtain enough dissolved oxygens and waste water is driven to flow, improve organic matter in waste water and microorganism and
The effect of dissolved oxygen contact guarantees that the organic matter in waste water under conditions of having sufficient dissolved oxygen, carries out oxidative decomposition,
It is secondary, it contacts sundries, microorganism and the dissolved oxygen etc. in waste water to form biomembrane with biologic packing material, it is organic to increase microbial degradation
The probability of pollutant extends the residence time of organic matter, enhanced biodegradation effect, by the organic matter of biologic packing material adsorption
Removal.
Agitation oxygen supply component include the stirring air inlet 10 being connected with the inside of left box body 2a and with stirring air inlet
Two groups of air stirring pipes 11 that mouth 10 is connected, by the way that waste water is entered left box body 2a from the water inlet pipe mouth 2d on left box body 2a
It is interior, it is passed through air into stirring air inlet 10 and two groups of air stirring pipes 11, comes into full contact with air with waste water, reaches aeration and increases
The effect of oxygen improves the processing reaction effect of postorder waste water and biologic packing material.
One group of third lacing wire steel pipe 12 being connected with the inner wall of main box 1 is equipped in two reaction chambers 5.
The working principle of the invention: by the way that waste water is entered in left box body 2a from the water inlet pipe mouth 2d on left box body 2a, to
It is passed through air in stirring air inlet 10 and two groups of air stirring pipes 11, air is come into full contact with waste water, reaches aeration oxygen replenishing
Effect improves the processing reaction effect of postorder waste water and biologic packing material, is carried out just using the first glass fiber reinforced grid-like panel 2c to waste water
Secondary filtering, plays dirty effect of blocking, and waste water is flowed into from the first hole to a reaction chamber 5 adjacent thereto again, wherein the first hole
Mouthful in the first screen frame 2f it is for re-filtering to waste water, make suspended matter and fine particle in waste water etc. can not with waste water into
Enter in reaction chamber 5, by being passed through air into two air inlets 7, and makes air in main gas tube 9a and several points of gas-guide tube 9b
Flow into two reaction chambers 5, while it is several revolve mixed aerator 9c work, so that waste water is obtained enough dissolved oxygens and drive
Waste water flowing improves the effect that the organic matter in waste water is contacted with microorganism and dissolved oxygen, guarantees that the organic matter in waste water is having
Under conditions of sufficient dissolved oxygen, oxidative decomposition is carried out, secondly, by sundries, microorganism and dissolved oxygen in waste water etc. and life
Object filler contacts to form biomembrane, increases the probability of microbial degradation organic pollutant, extends the residence time of organic matter, strengthens
Biodegradation, by the organic matter removal of biologic packing material adsorption, sewage draining exit and two exhaust pipes 8 can be in reaction points
The gas and sludge not generated are discharged, and are stopped by the second glass fiber reinforced grid-like panel 4b to biologic packing material, and waste water is from
Three hole 4d enter another reaction chamber 5, realize the secondary treatment technique of waste water, reach the processing mesh of high efficiency and high effect
, blocking filtering is carried out to the biologic packing material of a reaction chamber 5 adjacent thereto using the second screen frame 3e in the second hole, is passed through
Water of crossing that treated is discharged from effluent pipe mouth 3c, wherein can using recycling effluent mouth 3d, reflux water inlet 2e and connecting pipe
Make waste water by secondary cycle handle, whole design of the present invention is reasonable in design, can to coking wastewater carry out quickly, efficiently and
Stable fluidization treatment requirement, fluidisation operation safety are stablized.
Finally, it should be noted that the above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Pipe present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that: its according to
So be possible to modify the technical solutions described in the foregoing embodiments, or to some or all of the technical features into
Row equivalent replacement；And these are modified or replaceed, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (7)
1. a kind of new bio fluidized bed for Treatment of Coking Effluent, it is characterised in that: including main box (1), water inlet component
(2) and outlet component (3), the main box (1) is in rectangular configuration, and water inlet component (2) and outlet component (3) are separately positioned on master
Two sides of cabinet (1), and being both connected with the inside of main box (1), the top of the main box (1) be equipped with inside it
Its inner space can be divided into two impartial reaction chambers (5) by the filter assemblies (4) being connected, interior be equipped with of main box (1)
Partition (6), the upper end of the partition (6) extends in filter assemblies (4), is filled in two reaction chambers (5) and waste water
The biologic packing material of phase reaction is respectively equipped with the air inlet (7) and two being connected with a reaction chamber (5) at the top of main box (1)
A exhaust pipe (8), is equipped with the aeration component (9) being connected with two air inlets (7) in two reaction chambers (5), it is described into
Component is supplied oxygen equipped with the agitation that a reaction chamber (5) adjacent thereto is connected in water assembly (2).
2. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: described
Water inlet component (2) includes left box body (2a) and four group of first lacing wire steel pipe (2b), and four group of first lacing wire steel pipe (2b) is from upper
It is successively set under and in left box body (2a), is located in the middle on one group of first lacing wire steel pipe (2b) and is fixed with the first glass reinforced plastic
Flase floor (2c), and every group of first lacing wire steel pipe (2b) includes several equidistant and in horizontally disposed first lacing wire steel
Pipe, left box body (2a) are equipped with the water inlet pipe mouth (2d) being connected with inside it and reflux water inlet (2e), left box body (2a) and master
Cabinet (1) is fixedly connected, and side wall of the left box body (2a) close to main box (1) is equipped with the first hole, in first hole
Equipped with the first screen frame (2f).
3. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: described
Outlet component (3) includes right case (3a) and four group of second lacing wire steel pipe (3b), and four group of second lacing wire steel pipe (3b) is from upper
It is successively set under and in right case (3a), and every group of second lacing wire steel pipe (3b) includes several equidistant and in level
The second lacing wire steel pipe being arranged, right case (3a) are equipped with the effluent pipe mouth (3c) and recycling effluent mouth being connected with inside it
(3d), right case (3a) are fixedly connected with main box (1), and side wall of the right case (3a) close to main box (1) is equipped with the
Two holes are equipped with the second screen frame (3e) in second hole, and recycling effluent mouth (3d) and reflux water inlet (2e) pass through connecting tube
Road is connected.
4. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: described
Filter assemblies (4) include second of the upper box (4a) being connected with two reaction chambers (5) and setting on main box (1) top
Glass fiber reinforced grid-like panel (4b), the top of main box (1) are equipped with two slots for fixing the both ends the second glass fiber reinforced grid-like panel (4b)
The upper section portion of steel (4c), partition (6) is equipped with third hole (4d).
5. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: described
Aeration component (9) includes main gas tube (9a) and several points of gas-guide tubes (9b), the both ends of main gas tube (9a) respectively with two into
Port (7) is connected, several points of gas-guide tubes (9b) be symmetricly set in two reaction chambers (5) and each divide gas-guide tube (9b) with
Main gas tube (9a) is connected, and each divides gas-guide tube (9b) to be provided with several revolve and mixes aerator (9c).
6. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: described
Agitation oxygen supply component include the stirring air inlet (10) being connected with the inside of left box body (2a) and with stirring air inlet (10) phase
Two groups of air stirring pipes (11) of connection.
7. a kind of new bio fluidized bed for Treatment of Coking Effluent according to claim 1, it is characterised in that: two
One group of third lacing wire steel pipe (12) being connected with the inner wall of main box (1) is equipped in the reaction chamber (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910305045.2A CN109867419A (en) | 2019-04-16 | 2019-04-16 | A kind of new bio fluidized bed for Treatment of Coking Effluent |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910305045.2A CN109867419A (en) | 2019-04-16 | 2019-04-16 | A kind of new bio fluidized bed for Treatment of Coking Effluent |
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| CN109867419A true CN109867419A (en) | 2019-06-11 |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104803474A (en) * | 2015-04-02 | 2015-07-29 | 江苏鑫林环保设备有限公司 | Biological fluidized bed device |
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| CN106430586A (en) * | 2016-10-27 | 2017-02-22 | 中国人民解放军后勤工程学院 | Enhanced nitrogen-removing A/O flow-separating biochemical pond |
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| CN104803474A (en) * | 2015-04-02 | 2015-07-29 | 江苏鑫林环保设备有限公司 | Biological fluidized bed device |
| CN105776570A (en) * | 2016-03-23 | 2016-07-20 | 煤科集团杭州环保研究院有限公司 | High-density biological thickening reactor and method using same to treat high-salinity high-ammonia-hydrogen organic chemical industrial wastewater |
| US20180079671A1 (en) * | 2016-09-21 | 2018-03-22 | Thomas Wang | Ecological biowater purification system |
| CN106430586A (en) * | 2016-10-27 | 2017-02-22 | 中国人民解放军后勤工程学院 | Enhanced nitrogen-removing A/O flow-separating biochemical pond |
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| CN208500672U (en) * | 2018-05-25 | 2019-02-15 | 北京华明广远环境科技有限公司 | Donkey-hide gelatin waste water treatment system |
| CN208500690U (en) * | 2018-06-26 | 2019-02-15 | 广东环维环保科技有限公司 | A kind of apparatus for treating carbonized waste water with multi task process technique |
| CN209778598U (en) * | 2019-04-16 | 2019-12-13 | 江苏鑫汇林环境工程有限公司 | Novel biological fluidized bed for coking wastewater treatment |
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