CN202016933U - Sewage treatment device - Google Patents
Sewage treatment device Download PDFInfo
- Publication number
- CN202016933U CN202016933U CN2011200985522U CN201120098552U CN202016933U CN 202016933 U CN202016933 U CN 202016933U CN 2011200985522 U CN2011200985522 U CN 2011200985522U CN 201120098552 U CN201120098552 U CN 201120098552U CN 202016933 U CN202016933 U CN 202016933U
- Authority
- CN
- China
- Prior art keywords
- housing
- pipe
- pad
- treating sewage
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model provides a sewage treatment device, which comprises a casing, a support plate, composite filling materials, a water inlet pipe, a water outlet pipe, a perforated aerator and an air supply device, wherein the composite filling materials are arranged in the casing. The sewage treatment device is characterized in that a center barrel is arranged in the casing, a water distributor and micro-electrolysis filling materials are arranged in the center barrel, the micro-electrolysis filling materials and the bottom of the center barrel are arranged on the support plate, the water inlet pipe is connected with the water distributor, an annular upwards opening water collection tank surrounds the upper periphery of the center barrel, one end of the water outlet pipe is connected with the water collection tank, the other end of the water outlet pipe is led out through passing through the casing, the lower side of the support plate is connected with a center flow guide tube with the open upper end and the open lower end, a medicine adding device is arranged in the center flow guide tube, a medicine adding pipe connected with the medicine adding device is led out from the upper part of the casing through upwards passing through the center tube, and the composite filling materials arranged in the casing surround the periphery of the center tube, are divided into an upper layer and a lower layer and are supported by the support plate. The sewage treatment device has the advantages that the structure is reasonable and compact, a micro-electrolysis technology, a biological treatment technology and a filter technology are organically combined, the outlet water quality is good, and the efficiency is high.
Description
Technical field
The utility model belongs to technical field of sewage, is a kind of apparatus for treating sewage specifically.
Background technology
The processing of industrial sewage is the focus of common concern, because of a great variety, the water yield of industrial sewage change greatly, high, the complicated component of water concentration, thereby intractability is big.Adopt at present mostly the combined treatment process of routine techniques, these technologies often long flow path, the transmittance process power consumption is big, running cost is high, is difficult to reach the ideal treatment effect.Particularly high salt high concentration organic sewage is the difficult point of handling always, and organic contamination substrate concentration height in the sewage, Stability Analysis of Structures, biochemical are poor, and common process is difficult to realize qualified discharge, and the processing cost height, brings great pressure for enterprise's " energy-saving and emission-reduction ".In addition, fast because of the product transformation that the market requirement causes, cause the sewage situation complicated more, original sewage disposal technology technology and facility are made the matter worse, therefore, be badly in need of the sewage disposal New Product of highly effective at present.
In the treatment technology of difficult degradation industrial sewage, micro electrolysis tech comes into one's own just day by day, be a kind of desirable technique of handling printing and dyeing, plating, papermaking, medicine, oil of mirbane, aniline, printed-wiring board (PWB), coking, herding, hydrogen peroxide chemical industry, petrochemical complex, rubber ingredients chemical industry at present and containing the phenyl ring chemical engineering sewage, it is having its distinctive feature aspect the colourity of removing high-concentration sewage and the reduction COD.Biologic treating technique is to utilize microbiological oxidation and adsorption to remove the mature technology of pollutent.For this reason, how to pass through reasonable structural design, micro electrolysis tech, biologic treating technique and filtering technique organically combined form a kind of new-type apparatus for treating sewage, maximization performance excellent characteristics separately make that its effluent quality is good, shock-resistant, adaptability is strong, management easy to operate, economical and practical.This is the technical task that the present technique field faces.
Summary of the invention
The utility model is the problem that exists at prior art, a kind of apparatus for treating sewage is provided, it is rational in infrastructure, compact, micro electrolysis tech and biologic treating technique and filtering technique are organically combined, effluent quality is good, processing efficiency is high, shock-resistant, adaptability is strong, cost is low, and is simple to operate, easy to maintenance.
The utility model adopts following technical scheme: a kind of apparatus for treating sewage, comprise housing, back up pad, the intravital compounded mix of shell, the outer water inlet pipe that is connected with housing of housing, rising pipe and air feeder, the boring aeration device is set between back up pad and the compounded mix, the boring aeration device is connected by the air feeder of air-supply duct with the outside, it is characterized in that being provided with in the described housing central cylinder, the central cylinder internal upper part is provided with water distributor, the bottom is provided with micro-electrolysis stuffing, the opening of described micro-electrolysis stuffing and central cylinder bottom is seated on the described back up pad, and described water inlet pipe is introduced in the central cylinder by housing top and linked to each other with water distributor; The water leg that has an annular to be open upwards formula is centered around central cylinder and is higher than around the top of compounded mix, and described rising pipe one end links to each other with water leg, and the rising pipe the other end passes housing and draws; Central draft tube is established in the back up pad below, the central draft tube upper and lower ends is opening, and the central draft tube upper end is connected with back up pad, is provided with a doser in the central draft tube, there is a chemical feed pipe that is connected with doser to be upward through central tube and draws, link to each other with the medicine machine of outside from housing top; The intravital compounded mix of described shell is looped around around the central cylinder and is divided into upper and lower two-layerly supported by back up pad.
To further improvement in the technical proposal: described micro-electrolysis stuffing is an iron-carbon micro-electrolysis filler.
To further improvement in the technical proposal: the lower floor that is looped around in the described housing in the compounded mix around the central cylinder is a biologic packing material, and the upper strata is the high-density fiber silk.
To further improvement in the technical proposal: described boring aeration device is an annular, is centered around around the central cylinder, is positioned at the below of the biologic packing material of lower floor, and on the air-supply duct that the boring aeration device is connected pressure lock is set.
To further improvement in the technical proposal: described doser is the annular perforations tubular type.
To further improvement in the technical proposal: described housing is circular cylindrical shell, and top is cylindrical, and the bottom be conical, described back up pad be arranged on housing cylindrical in, by 4 uniform in housing taper shape bracing frames supports.
To further improvement in the technical proposal: the most advanced and sophisticated shore pipe that connects of described housing bottom, connect a blow-down pipe on the shore pipe, the emptying magnetic valve is set on the blow-down pipe, soil discharging electromagnetic valve is set on the shore pipe.During works better, soil discharging electromagnetic valve and emptying closed electromagnetic valve are just opened soil discharging electromagnetic valve when needing spoil disposal; During maintenance, soil discharging electromagnetic valve is closed, and the emptying magnetic valve is opened.
The utility model compared with prior art has the following advantages and positively effect:
The utility model apparatus for treating sewage design science, rational in infrastructure is handled micro electrolysis tech, flocculation sediment technology, biological iron processes technology, microbial film and filtering technique combines, thereby has following advantage:
1, efficient height, cost is low: the utility model is finished the multiple actions such as electrochemistry, oxidation-reduction, physical adsorption, flocculation sediment, biological absorption, bio-oxidation and filtration to sewage in same tank body, speed of reaction is fast, the processing efficiency height, cost is low;
2, applied range, removing degradation of organic substances matter etc. as: the difficulty that contains the two keys of even fluorine, carbon, nitro, halogeno-group structure all has good degradation effect;
3, few, the convenient operating maintenance of micro-electrolysis stuffing long service life, investment cost, running cost is low, treatment effect is stable.Only consume a spot of micro-electrolysis reaction agent in the treating processes.Fine electrolyser only needs regularly to add and need not to change, and interpolation also need not to activate direct input and gets final product;
4, sewage can form the ferrous or iron ion of ecosystem in water after little electrolysis treatment, has than the effect of common coagulants better coagulation, need not to add coagulating agent such as molysite again, colourity, COD clearance height, and can not cause secondary pollution to water; Can improve simultaneously the biodegradability of sewage to a great extent.Can reach the effect of chemical precipitation dephosphorization, can also remove heavy metal by reduction;
5, aeration rate is little, and power consumption is low;
6, rational in infrastructure, compact, reduced investment, floor space is little
7, capacity of resisting impact load is strong;
8, easy for installation, the later stage reorganization and expansion is convenient in the easy handling management.
9, both can be used for newly-built sewage treatment project, also can be used for building up the transformation of below standard high concentration organic sewage treatment project.
Description of drawings
Fig. 1 is the johning knot composition of the utility model apparatus for treating sewage.
Among the figure: 1, water inlet pipe; 2, housing; 3, high-density fiber silk; 4 biologic packing materials; 5, air-supply duct; 6, pressure lock; 7, water distributor; 8, iron-carbon micro-electrolysis filler; 9, central cylinder; 10, doser; 11, central draft tube; 12, bracing frame; 13, chemical feed pipe; 14, water leg; 15, rising pipe; 16, boring aeration device; 17, back up pad; 18, emptying magnetic valve; 19, blow-down pipe; 20, soil discharging electromagnetic valve; 21, shore pipe.
Embodiment
Below in conjunction with accompanying drawing the utility model is further described.
Referring to Fig. 1, the embodiment of a kind of apparatus for treating sewage of the utility model, housing 2 is done circular cylindrical shell by certain thickness steel plate (as: carbon steel adds the glass steel or stainless steel), and top is cylindrical, and the bottom is conical, and by base supports.Have a back up pad 17 be arranged on housing 2 cylindrical in, in the bottom of back up pad 17 4 uniform bracing frames 12 are set, bracing frame 12 upper ends link to each other with back up pad 17, the lower end links to each other with housing 2 bottoms.
In the middle of in housing 2 central cylinder 9 is set, the equal opening of central cylinder 9 upper and lower ends is equipped with the micro-electrolysis stuffing of iron-carbon micro-electrolysis filler 8 or other similarities, and places on the back up pad 17 in the central cylinder 9.On back up pad 17, have permeable hole, and to cover the permeable aperture of part little in central cylinder 9 lower ends, big around the permeable aperture of central cylinder 9 lower port parts.Establish water distributor 7 above the iron-carbon micro-electrolysis filler 8 in central cylinder 9, water distributor 7 is annular perforations tubular type or spray-type, has an end of a water inlet pipe 1 that is connected with water distributor 7 to draw housing 2 outsides, and is arranged on the top of housing 2.Annular space in housing 2 is equipped with compounded mix, and compounded mix is looped around around the central cylinder 9, and two-layer about being divided into, and the upper strata is a high-density fiber silk 3, and lower floor is a biologic packing material 4, is supported by back up pad 17.High-density fiber silk 3 tops are provided with the water leg 14 that an annular is open upwards formula and are looped around around the central cylinder 9, have rising pipe 15 1 ends that are connected with water leg 14 to draw housing 2 outsides, and are arranged on the housing 2 columniform sidewalls.The bottom of biologic packing material 4 is provided with annular boring aeration device 16, is centered around around the central cylinder 9, and boring aeration device 16 is connected by the air feeder of air-supply duct 5 with the outside.The air feed equipment of air feeder adopts air compressor machine, and pressure lock 6 is set on the air-supply duct 5, can be microorganism oxygen source is provided, and rise and stir regeneration function, regulates air demand according to different needs.
Establish central draft tube 11 below back up pad 17, central draft tube 11 upper and lower ends are opening, and central draft tube 11 upper ends are connected with back up pad 17, are provided with a doser 10 in the central draft tube 11, and doser 10 is the annular perforations tubular type.There is a chemical feed pipe 13 that is connected with doser 10 to be upward through central cylinder 9 and draws, link to each other with the medicine machine of outside from housing 2 tops.
Connect a shore pipe 21 in housing 2 bottom tip, connect a blow-down pipe 19 on the shore pipe 21, emptying magnetic valve 18 is set on the blow-down pipe 19, soil discharging electromagnetic valve 20 is set on the shore pipe 21.
The processing mechanism of the utility model apparatus for treating sewage:
A. redoxomorphism
When effluent stream when containing iron-carbon micro-electrolysis filler 8 owing to have difference in Electrode Potential between Fe and the C, thereby can form countless microbattery systems, do not need the additional power source just can be at electric field of its action space formation.Iron is anode, carbon is negative electrode, the nascent state ferrous ion that anodic reaction produces has stronger reducing power, can make some organism reduction, (the two keys as carboxyl-COOH, azo-group-N=N-) are opened also can to make some unsaturated group, make part difficult degradation ring-type and long-chain organism resolve into the small organic molecule of readily biodegradable and improve biodegradability, Fe
2+Reductibility can be reduced into the little or nontoxicity material of toxicity to deleterious compound or ion.Cathodic reaction produces a large amount of nascent states [H] and [O], under the condition of slant acidity, these activeconstituentss all can with the many component generation redox reactions in the sewage, make organic macromolecule generation chain-scission degradation, thereby eliminated the colourity of organic sewage, improved the biodegradability of sewage.
B. throwing out
Divalence and ferric ion that microbattery produces are good flocculation agents, and particularly Xin Sheng ferrous ion has higher absorption-flocculation activity, need not to add coagulating agent such as molysite again.The pH that regulates sewage can make iron ion become the flocks of oxyhydroxide, and the suspension in the absorption sewage or the molecule and the organic polymer of colloidal attitude can further reduce the colourity of sewage, remove the part organic pollution materials simultaneously sewage is purified.
C. biological iron effect
In the microbattery reaction, redox reaction takes place under certain condition and transforms mutually in ferrous iron and ferric iron.Research finds that some bacterium can obtain nutriment from the chemical reaction of iron, and these bacteriums can consume the compound such as acetate and lactic acid that produces when microorganism is rotted in ferric iron and ferrous iron conversion process.The energy force rate methanogen and the sulphate reducing bacteria that also confirm these bacterial degradation organic matters are all much better than, as long as there is iron to exist, always that iron-reducing bacterium at first is reduced into positive iron is ferrous, and drive other bacteria breeds procreations.
Ferrous iron and ferric redox reaction can promote the degraded of bacterium to the organic suspension thing.Biooxidation reactions mostly is the dehydrogenation oxidation, organism is not directly to give Sauerstoffatom hydrogen atom, but under the effect of deoxygenase and various coenzyme, transmit through a series of hydrogen donors, again hydrogen atom is passed to cytopigment, cytopigment and iron ion complex reaction are finally given molecular oxygen proton and electronics as the carrier of proton and electronics, carry out complete oxidation.
Iron can reduce the activation energy of microorganism growth activation energy and substrate degradation reaction, thereby weakens the influence that reaction process is subjected to external environment factors such as temperature, accelerates organic matter degradation rate and microorganisms grow speed.
D. bio-oxidation
Microbial film in biologic packing material 4 surface growths of this apparatus for treating sewage, because the specific surface area of biologic packing material 4 is big, so the big concentration height of biofilm biomass.When the sewage of handling through micro-electrolysis stuffing 8 entered biologic packing material 4, the metabolic activity oxidation removal pollutent because of the microorganism on the biologic packing material 4 was purified sewage.By airing system it is carried out aeration,, stir simultaneously, impel microbial film to bring in constant renewal in, make microbial film remain the high reactivity operation for microorganism provides oxygen.
E. biological adsorption
The viscous substance that microorganism produces in metabolism, play the adsorption bridging effect as polyose, ester class etc., bond together with suspended particle and colloidal particle, form tiny flco, adsorption mainly utilizes flocs unit to finish, the flocculation physical efficiency make the organism of suspensions a large amount of in the sewage be attached on it above, decomposed utilization then.Bacterium in the flocs unit just can not be engulfed by protozoon owing to be embedded in the colloid, flocs unit be formed with the sedimentation that is beneficial to mud.Therefore highly active microbial film not only is embodied in bio-oxidation, degraded aspect, more shows as biofloculation, adsorption, to the material of some difficult degradations, it can be adsorbed, is trapped in wherein, is removed.
F. filteration
The high-density fiber silk 3 of this apparatus for treating sewage is as filler, and the many specific surface areas in its space are big, have the mechanical retention effect, can hold back suspended substance and biological floe in the sewage in large quantities, and the one, guarantee effluent quality, the 2nd, keep activated sludge concentration.
The principle of work of the utility model apparatus for treating sewage:
Water inlet is entered in the internal layer central cylinder 9 of apparatus for treating sewage by water inlet pipe 1, behind water distributor 7 water distribution uniformities, flow into iron-carbon micro-electrolysis filler 8 zones downwards, because iron in the iron-carbon micro-electrolysis filler 8, the redoxomorphism of the microbattery that carbon forms, the acting in conjunction of physical adsorption and flocculation sediment is handled sewage, remove heavy metal, toxic pollutants, phosphorus etc., and the biodegradability of raising sewage, water after the processing in central draft tube 11 after the pH of doser 10 adjusts, mud-water separation is carried out in the disengaging zone that enters central draft tube 11 bottoms, mud enters the conical portion of housing 2 bottoms, discharges through the shore pipe 21 of soil discharging electromagnetic valve 20 controls.Water utilizes the microbial film of growing on the biologic packing material 4 sewage to be carried out effects such as bio-oxidation, biological absorption and biofloculation and purifies water then by upwards entering biologic packing material 4 zones around the central draft tube 11.The required oxygen of microorganism is carried through perforated pipe aerator 16 by air-supply duct 5 by air compressor machine, and air capacity is by pressure lock 6 controls.Then, water continues upwards to enter high-density fiber silk 3 zones, utilize impurity such as suspended substance in 3 pairs of water of high-density fiber silk and biological floe to hold back, filter, guarantee effluent quality, final treat effluent is collected by the rising pipe 15 that penetrates housing 2 through the water leg 14 of top and is discharged, and the entire treatment process is finished.During works better, emptying magnetic valve 18 cuts out, and when having only equipment to overhaul, emptying magnetic valve 18 is just opened.
The utility model apparatus for treating sewage is mainly used in industrial sewage and handles.
Certainly, above-mentioned explanation is not to be to restriction of the present utility model, and the utility model is not limited to above-mentioned giving an example; those skilled in the art; in essential scope of the present utility model, the variation of making, remodeling, interpolation or replacement all should belong to protection domain of the present utility model.
Claims (10)
1. apparatus for treating sewage, comprise housing, back up pad, the intravital compounded mix of shell, the outer water inlet pipe that is connected with housing of housing, rising pipe and air feeder, the boring aeration device is set between back up pad and the compounded mix, the boring aeration device is connected by the air feeder of air-supply duct with the outside, it is characterized in that being provided with in the described housing central cylinder, the central cylinder internal upper part is provided with water distributor, the bottom is provided with micro-electrolysis stuffing, the opening of described micro-electrolysis stuffing and central cylinder bottom is seated on the described back up pad, and described water inlet pipe is introduced in the central cylinder by housing top and linked to each other with water distributor; The water leg that has an annular to be open upwards formula is centered around central cylinder and is higher than around the top of compounded mix, and described rising pipe one end links to each other with water leg, and the rising pipe the other end passes housing and draws; Central draft tube is established in the back up pad below, the central draft tube upper and lower ends is opening, and the central draft tube upper end is connected with back up pad, is provided with a doser in the central draft tube, there is a chemical feed pipe that is connected with doser to be upward through central tube and draws, link to each other with the medicine machine of outside from housing top; The intravital compounded mix of described shell is looped around around the central cylinder and is divided into upper and lower two-layerly supported by back up pad.
2. according to the described apparatus for treating sewage of claim 1, it is characterized in that described micro-electrolysis stuffing is an iron-carbon micro-electrolysis filler.
3. according to claim 1 or 2 described apparatus for treating sewage, it is characterized in that the lower floor that is looped around in the described housing in the central cylinder compounded mix on every side is a biologic packing material, the upper strata is the high-density fiber silk.
4. according to the described apparatus for treating sewage of claim 3, it is characterized in that described boring aeration device for annular, is centered around around the central cylinder, be positioned at the below of the biologic packing material of lower floor, and on the air-supply duct that the boring aeration device is connected pressure lock is set.
5. according to claim 1 or 2 described apparatus for treating sewage, it is characterized in that described doser is the annular perforations tubular type.
6. according to the described apparatus for treating sewage of claim 4, it is characterized in that described doser is the annular perforations tubular type.
7. according to claim 1 or 2 described apparatus for treating sewage, it is characterized in that described housing is circular cylindrical shell, top is cylindrical, the bottom be conical, described back up pad be arranged on housing cylindrical in, by 4 uniform in housing taper shape bracing frames supports.
8. according to the described apparatus for treating sewage of claim 6, it is characterized in that described housing is circular cylindrical shell, top is cylindrical, the bottom be conical, described back up pad be arranged on housing cylindrical in, by 4 uniform in housing taper shape bracing frames supports.
9. according to the described apparatus for treating sewage of claim 7, it is characterized in that the most advanced and sophisticated shore pipe that connects of described housing bottom, connect a blow-down pipe on the shore pipe, the emptying magnetic valve is set on the blow-down pipe, soil discharging electromagnetic valve is set on the shore pipe.
10. according to the described apparatus for treating sewage of claim 8, it is characterized in that the most advanced and sophisticated shore pipe that connects of described housing bottom, connect a blow-down pipe on the shore pipe, the emptying magnetic valve is set on the blow-down pipe, soil discharging electromagnetic valve is set on the shore pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200985522U CN202016933U (en) | 2011-03-25 | 2011-03-25 | Sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200985522U CN202016933U (en) | 2011-03-25 | 2011-03-25 | Sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202016933U true CN202016933U (en) | 2011-10-26 |
Family
ID=44810607
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200985522U Expired - Lifetime CN202016933U (en) | 2011-03-25 | 2011-03-25 | Sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202016933U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102134145A (en) * | 2011-03-25 | 2011-07-27 | 青岛赛尔环境保护有限公司 | Sewage treatment device |
| CN103073165A (en) * | 2013-02-20 | 2013-05-01 | 青岛赛尔环境保护有限公司 | Chemical and biological sewage treatment device |
| CN104192869A (en) * | 2014-08-25 | 2014-12-10 | 湖南江冶机电科技股份有限公司 | Purification method and device of desulfurization lead plaster filtrate |
| CN104528993A (en) * | 2014-12-18 | 2015-04-22 | 湖北师范学院 | Method for treating arsenic-containing wastewater by use of SO2 in flue gas |
| CN104925939A (en) * | 2015-07-15 | 2015-09-23 | 湖北泉盛环保科技有限公司 | Moving bed bio-membrane reactor |
| CN105417657A (en) * | 2015-12-16 | 2016-03-23 | 苏州捷宁模塑有限公司 | Filler structure of electronic complexing wastewater treatment tank |
| CN105540826A (en) * | 2015-12-16 | 2016-05-04 | 苏州捷宁模塑有限公司 | Filling material structure for rice factory sewage treatment |
| CN105906107A (en) * | 2016-06-28 | 2016-08-31 | 董超超 | Domestic sewage treatment device |
| CN114180711A (en) * | 2021-12-08 | 2022-03-15 | 西安聚光环保科技有限公司 | Biochemical treatment device for high-salt-content wastewater |
-
2011
- 2011-03-25 CN CN2011200985522U patent/CN202016933U/en not_active Expired - Lifetime
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102134145A (en) * | 2011-03-25 | 2011-07-27 | 青岛赛尔环境保护有限公司 | Sewage treatment device |
| CN102134145B (en) * | 2011-03-25 | 2012-09-26 | 青岛赛尔环境保护有限公司 | Sewage treatment device |
| CN103073165A (en) * | 2013-02-20 | 2013-05-01 | 青岛赛尔环境保护有限公司 | Chemical and biological sewage treatment device |
| CN103073165B (en) * | 2013-02-20 | 2014-10-08 | 青岛赛尔环境保护有限公司 | Chemical and biological sewage treatment device |
| CN104192869A (en) * | 2014-08-25 | 2014-12-10 | 湖南江冶机电科技股份有限公司 | Purification method and device of desulfurization lead plaster filtrate |
| CN104528993A (en) * | 2014-12-18 | 2015-04-22 | 湖北师范学院 | Method for treating arsenic-containing wastewater by use of SO2 in flue gas |
| CN104925939A (en) * | 2015-07-15 | 2015-09-23 | 湖北泉盛环保科技有限公司 | Moving bed bio-membrane reactor |
| CN104925939B (en) * | 2015-07-15 | 2017-03-08 | 湖北泉盛环保科技股份有限公司 | A kind of MBBR |
| CN105417657A (en) * | 2015-12-16 | 2016-03-23 | 苏州捷宁模塑有限公司 | Filler structure of electronic complexing wastewater treatment tank |
| CN105540826A (en) * | 2015-12-16 | 2016-05-04 | 苏州捷宁模塑有限公司 | Filling material structure for rice factory sewage treatment |
| CN105906107A (en) * | 2016-06-28 | 2016-08-31 | 董超超 | Domestic sewage treatment device |
| CN114180711A (en) * | 2021-12-08 | 2022-03-15 | 西安聚光环保科技有限公司 | Biochemical treatment device for high-salt-content wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202016933U (en) | Sewage treatment device | |
| CN102134145B (en) | Sewage treatment device | |
| CN105753270B (en) | A kind of water purification system suitable for high ammonia nitrogen livestock breeding wastewater | |
| CN107698037B (en) | Method for deeply treating reverse osmosis concentrated water of landfill leachate by three-dimensional electrochemical coupling three-dimensional electrobiology | |
| CN103086574B (en) | Aquatic product processing wastewater treatment equipment | |
| CN101538100A (en) | Method for treating dyeing wastewater and dedicated device | |
| CN205773937U (en) | A kind of ozone occurs and processing means | |
| CN108373203A (en) | Autotrophic denitrification membrane bioreactor | |
| CN113307456A (en) | Improved sewage treatment method and device for MBBR (moving bed biofilm reactor) process | |
| CN101676230A (en) | Integral processing method for industrial waste water by catalyzed iron internal electrolysis and suspended carrier bio-film | |
| CN106336078A (en) | Chemical wastewater treatment system and chemical wastewater treatment method | |
| CN203159389U (en) | Aquatic product processing wastewater treatment equipment | |
| CN103102046B (en) | Biochemical strengthening processor | |
| CN101200331B (en) | Method for producing reclaimed water by membrane bioreactor-ozone combination technique | |
| CN202988918U (en) | Multi-stage multi-section combined type high concentration chemical wastewater treatment system | |
| CN206051804U (en) | Chemical wastewater treatment system | |
| CN202543002U (en) | Sewage treatment system | |
| CN204874204U (en) | Chloroprene rubber effluent disposal system | |
| CN106865769A (en) | High-concentration organic wastewater purification device and purification method | |
| CN112624500B (en) | Kitchen waste sewage treatment system and method | |
| CN205088072U (en) | Sewage treating and filtering device | |
| CN212269816U (en) | Aged landfill leachate non-concentrated solution treatment system | |
| CN203065309U (en) | biochemical strengthening processor | |
| CN211226789U (en) | Hardly biodegradable organic wastewater treatment equipment | |
| CN208454616U (en) | A kind of autotrophic denitrification membrane bioreactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20111026 Effective date of abandoning: 20120926 |