CN107226579A - A kind of sewage disposal device - Google Patents
A kind of sewage disposal device Download PDFInfo
- Publication number
- CN107226579A CN107226579A CN201610171142.3A CN201610171142A CN107226579A CN 107226579 A CN107226579 A CN 107226579A CN 201610171142 A CN201610171142 A CN 201610171142A CN 107226579 A CN107226579 A CN 107226579A
- Authority
- CN
- China
- Prior art keywords
- bucket
- sewage disposal
- pump
- anaerobic reation
- disposal device
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Abstract
The present invention proposes a kind of sewage disposal device, bucket is adjusted including PH, the one-level elevator pump connected at the top of bucket is adjusted with PH, the reaction container that bottom of the barrel is connected is adjusted with PH, the plate and frame filter press connected by pneumatic diaphragm pump with reaction bottom of the barrel, the Distallation systm connected with plate and frame filter press, the biochemical regulating reservoir that top is connected by two-stage hoisting pump with Distallation systm, the anaerobic reation pool that top is connected by three-level elevator pump with biochemical regulating reservoir bottom, the contact-oxidation pool that top is connected with anaerobic reation pool bottom, the aerated precipitation tank that top is connected with contact-oxidation pool bottom, the filtering bucket that top is connected with aerated precipitation tank bottom, the mechanical filter connected by filter pump with filtering bucket top.The present invention realizes automatic grain slag separation by rational pipe design, and largely using polypropylene plastics as the material of sewage disposal container, not only corrosion resistance is good, and engineering construction cost is relatively low, high financial profit and easy large-scale promotion.
Description
Technical field
The present invention relates to sewage treatment area, more particularly to a kind of sewage disposal device.
Background technology
Water resource is the indispensable important natural resources of developing national economy.
Water is once contaminated, it will be difficult to recycled.With China's rapid development of economy, sanitary sewage, the discharge capacity of trade effluent are also continuously increased, if these sewage are effectively handled not in time, the water resource to the Nature are polluted, ecological environment will be seriously damaged.
Existing sewage disposal device, can be to a certain extent sewage purification into water up to standard, but its floor space is big, engineering construction cost is high, and purification speed is slower, and the sludge in pond needs regular manual cleaning, the material resources that not only waste financial resources manpower, the construction of semiworks is not suitable for also.
The content of the invention
The present invention is big for sewage disposal device floor space in the prior art, engineering construction cost is high, sewage purification speed is slow, the shortcomings of sludge needs manual cleaning, it is small there is provided a kind of floor space, engineering construction cost is relatively low, and sewage purification speed is fast, and without the sewage disposal device of manual cleaning pond sludge.
In order to solve the above-mentioned technical problem, the present invention is addressed by following technical proposals：
Sewage disposal device, bucket is adjusted including PH, the one-level elevator pump connected at the top of bucket is adjusted with PH, the reaction container that bottom of the barrel is connected is adjusted with PH, the plate and frame filter press connected by pneumatic diaphragm pump with reaction bottom of the barrel, the Distallation systm connected with plate and frame filter press, the biochemical regulating reservoir that top is connected by two-stage hoisting pump with Distallation systm, the anaerobic reation pool that top is connected by three-level elevator pump with biochemical regulating reservoir bottom, the contact-oxidation pool that top is connected with anaerobic reation pool bottom, the aerated precipitation tank that top is connected with contact-oxidation pool bottom, the filtering bucket that top is connected with aerated precipitation tank bottom, the mechanical filter connected by filter pump with filtering bucket top, the mechanical filter is provided with a floss hole.
Further, the Distallation systm includes waste gas liquid collecting vessel and distillation case, distillation case is connected with waste gas liquid collecting vessel, the distillation case is provided with a blower fan with waste gas liquid collecting vessel connectivity part, heater is provided with the distillation case, the distillation bucket is connected with the plate and frame filter press, two-stage hoisting pump.
Further, the PH regulations bucket is two, is respectively designated as the first PH regulation buckets and the 2nd PH regulations, and the first PH adjusts bottom of the barrel and connected by water pipe with the 2nd PH regulations top.
Further, the anaerobic reation pool quantity is two, is respectively designated as the first anaerobic reation pool and the second anaerobic reation pool, the first anaerobic reation pool bottom is by water pipe with being connected at the top of the second anaerobic reation pool.
Further, roots blower is provided with the contact-oxidation pool.
Further, in addition to sludge barrel, the sludge barrel is connected with the aerated precipitation tank.
Further, the aerated precipitation tank is also connected with the anaerobic reation pool.
The present invention is as a result of above technical scheme, with significant technique effect：
1st, the present invention it is a large amount of using polypropylene plastics charging baskets as sewage disposal container, not only corrosion resistance is good, can also high concentration put, reduce occupation area of equipment.
2nd, full-automatic the dirty water decontamination handles are can be achieved in the present invention, and the sludge of reaction container precipitation is directly pumped into plate and frame filter press by pneumatic diaphragm pump and carries out solid and liquid separation, the sludge precipitated without manual cleaning reaction container.
3rd, the present invention is provided with roots blower in contact-oxidation pool so that oxygen-containing air can be constantly drawn into decomposes with sewage bump contact, acceleration biological oxidation, accelerates sewage purification speed.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention.
Embodiment
The present invention is described in further detail with embodiment below in conjunction with the accompanying drawings.
Embodiment
As shown in Figure 1, sewage disposal device, bucket is adjusted including PH, the one-level elevator pump connected at the top of bucket is adjusted with PH, the reaction container that bottom of the barrel is connected is adjusted with PH, the plate and frame filter press connected by pneumatic diaphragm pump with reaction bottom of the barrel, the Distallation systm connected with plate and frame filter press, the biochemical regulating reservoir that top is connected by two-stage hoisting pump with Distallation systm, the anaerobic reation pool that top is connected by three-level elevator pump with biochemical regulating reservoir bottom, the contact-oxidation pool that top is connected with anaerobic reation pool bottom, the aerated precipitation tank that top is connected with contact-oxidation pool bottom, the filtering bucket that top is connected with aerated precipitation tank bottom, the mechanical filter connected by filter pump with filtering bucket top, the mechanical filter is provided with a floss hole；The Distallation systm includes waste gas liquid collecting vessel and distillation case, distillation case is connected with waste gas liquid collecting vessel, distill case to be provided with a blower fan, the distillation case provided with heater with waste gas liquid collecting vessel connectivity part, the distillation bucket is connected with the plate and frame filter press, two-stage hoisting pump；The PH regulations bucket is two, is respectively designated as the first PH regulation buckets and the 2nd PH regulations, and the first PH adjusts bottom of the barrel and connected by water pipe with the 2nd PH regulations top；The anaerobic reation pool quantity is two, is respectively designated as the first anaerobic reation pool and the second anaerobic reation pool, the first anaerobic reation pool bottom is by water pipe with being connected at the top of the second anaerobic reation pool；Roots blower is provided with the contact-oxidation pool；Also include sludge barrel, the sludge barrel is connected with the aerated precipitation tank；The aerated precipitation tank is also connected with the anaerobic reation pool.
The workflow of sewage disposal device of the present invention is：
Sewage is pumped into PH regulation buckets by a, one-level elevator pump, the PH of sewage is adjusted using NaOH or balanced.B, PH regulate rear sewage and enter reaction container, using PAC, PAM to coagulation sedimentations such as the particles that is suspended in sewage；C, after the coagulation sedimentation in reaction container, then plate and frame filter press be pumped into by pneumatic diaphragm carry out solid and liquid and separate；D, the sewage liquid separated by plate and frame filter press enter distillation bucket and heated, and evaporate the volatile small organic molecule such as ethanol, then be collected into waste gas liquid collecting vessel by the rotation of blower fan；E, sewage are pumped into biochemical regulating reservoir by two-stage hoisting again and carry out the regulation such as water temperature；F, again by three-level lifting be pumped into anaerobic reation pool, using the effect of anaerobic bacteria, hydrolyze organic matter；G, contact-oxidation pool is flowed into again, oxygen-containing air is pumped into sewage and accelerates biological oxidation and decompose using roots blower；H, aerated precipitation tank is flowed into again carrying out sludge settling, unnecessary sludge is directly discharged into sludge barrel, and excess sludge is discharged into anaerobic reation pool again again；I, sewage flow into filtering bucket and filtered again；J, then again by filtering be pumped into mechanical filter carry out reprecipitation filtering；K and then water up to standard is directly discharged by floss hole.
In a word, presently preferred embodiments of the present invention is the foregoing is only, all equivalent changes and modifications made according to scope of the present invention patent should all belong to the covering scope of patent of the present invention.
Claims (7)
1. sewage disposal device, it is characterised in that：Bucket is adjusted including PH, adjust what is connected at the top of bucket with PH
One-level elevator pump, with PH adjust bottom of the barrel connect reaction container, pass through pneumatic diaphragm pump with reaction bottom of the barrel company
Logical plate and frame filter press, the Distallation systm connected with plate and frame filter press, top pass through two-stage hoisting pump and distillation
The anaerobism that the biochemical regulating reservoir of system connectivity, top are connected by three-level elevator pump with biochemical regulating reservoir bottom is anti-
Contact-oxidation pool that Ying Chi, top are connected with anaerobic reation pool bottom, top are connected with contact-oxidation pool bottom
Aerated precipitation tank, top connected with aerated precipitation tank bottom filtering bucket, by filter pump and filter water
The mechanical filter of bucket top connection, the mechanical filter is provided with a floss hole.
2. the sewage disposal device according to claim 1, it is characterised in that：The Distallation systm bag
Waste gas liquid collecting vessel and distillation case are included, distillation case is connected with waste gas liquid collecting vessel, the distillation case and waste gas
Liquid collecting vessel connectivity part is provided with a blower fan, is provided with heater in the distillation case, and the distillation bucket is and institute
State plate and frame filter press, the connection of two-stage hoisting pump.
3. the sewage disposal device according to claim 1, it is characterised in that：The PH adjusts bucket
For two, the first PH regulation buckets and the 2nd PH regulations are respectively designated as, the first PH regulations bottom of the barrel passes through
Water pipe is connected with the 2nd PH regulations top.
4. the sewage disposal device according to claim 1, it is characterised in that：The anaerobic reation pool
Quantity is two, is respectively designated as the first anaerobic reation pool and the second anaerobic reation pool, the first anaerobic reation pool
Bottom is by water pipe with being connected at the top of the second anaerobic reation pool.
5. the sewage disposal device according to claim 1, it is characterised in that：The contact-oxidation pool
It is interior to be provided with roots blower.
6. the sewage disposal device according to claim 1, it is characterised in that：Also include sludge barrel,
The sludge barrel is connected with the aerated precipitation tank.
7. the sewage disposal device according to claim 1, it is characterised in that：The aerated precipitation tank
Also connected with the anaerobic reation pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610171142.3A CN107226579A (en) | 2016-03-24 | 2016-03-24 | A kind of sewage disposal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610171142.3A CN107226579A (en) | 2016-03-24 | 2016-03-24 | A kind of sewage disposal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107226579A true CN107226579A (en) | 2017-10-03 |
Family
ID=59932721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610171142.3A Pending CN107226579A (en) | 2016-03-24 | 2016-03-24 | A kind of sewage disposal device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107226579A (en) |
Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4212456A1 (en) * | 1992-04-14 | 1993-10-21 | Cc & C Bioservice Gmbh Abwasse | Recycling of used fats contg. water, esp. from fat-water separators - includes mixing and sedimenting fat, further separating at specific temp. and filtering and vacuum-distilling |
| JP2000263080A (en) * | 1999-03-17 | 2000-09-26 | Kawasaki Steel Corp | Treatment method for organic-containing alkaline waste liquid |
| US20050131086A1 (en) * | 2002-06-18 | 2005-06-16 | Dancuart Kohler Luis P.F. | Method of purifying fischer-tropsch derived water |
| CN1654352A (en) * | 2005-01-06 | 2005-08-17 | 重庆大学 | System and method for urban sewage chemical-biologic composite deep phosphorous removal |
| CN1966428A (en) * | 2006-10-16 | 2007-05-23 | 西安长庆科技工程有限责任公司 | Gas field methanol sewage disposal process |
| US20080023407A1 (en) * | 2003-12-17 | 2008-01-31 | Denis ANGELERI | Water Treatment Process |
| CN101250017A (en) * | 2008-04-02 | 2008-08-27 | 总装备部工程设计研究总院 | Purification technique for methyl stannum mercaptide industrial sewage |
| CN101549938A (en) * | 2009-04-29 | 2009-10-07 | 浙江商达水务有限公司 | Method for treating waste water containing high concentration of organosilicon |
| CN102001794A (en) * | 2010-11-30 | 2011-04-06 | 华东理工大学 | Method for treating unsaturated polyester resin production wastewater |
| CN202390289U (en) * | 2011-12-21 | 2012-08-22 | 江阴明大化工有限公司 | Device for treating unsaturated polyester process wastewater efficiently |
| CN102976543A (en) * | 2012-12-18 | 2013-03-20 | 深圳市能源环保有限公司 | Garbage leachate disposal method and system |
| CN103482715A (en) * | 2013-09-16 | 2014-01-01 | 惠州Tcl环境科技有限公司 | High-concentration organic waste water evaporating and concentration processing method |
| CN103588356A (en) * | 2013-10-17 | 2014-02-19 | 东莞云水谣环保科技有限公司 | Combination system for treating landfill leachate and method for treating landfill leachate by using combination system |
| CN103601616A (en) * | 2013-11-20 | 2014-02-26 | 杭州上一环保技术有限公司 | Alcohol-water separation recycling method of fischer-tropsch synthesis reaction water |
| CN104609665A (en) * | 2015-01-21 | 2015-05-13 | 四川省环境保护科学研究院 | Glyphosate-producing wastewater treatment integration technology |
| CN204779248U (en) * | 2015-06-16 | 2015-11-18 | 大连广泰源环保科技有限公司 | A sewage treatment system for landfill leachate |
| CN204958664U (en) * | 2015-08-26 | 2016-01-13 | 合肥中盛水务发展有限公司 | Processing system of medicine waste water |
| CN105254141A (en) * | 2015-11-24 | 2016-01-20 | 广东先导稀材股份有限公司 | Treatment method and treatment system for high-concentration mixed salt organic wastewater |
| CN105366863A (en) * | 2015-11-24 | 2016-03-02 | 山东东岳氟硅材料有限公司 | High-efficient eco-friendly processing method for reducing COD in sewage |
| CN205556392U (en) * | 2016-03-24 | 2016-09-07 | 福建省三净环保科技有限公司 | Sewage treatment equipment |
-
2016
- 2016-03-24 CN CN201610171142.3A patent/CN107226579A/en active Pending
Patent Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4212456A1 (en) * | 1992-04-14 | 1993-10-21 | Cc & C Bioservice Gmbh Abwasse | Recycling of used fats contg. water, esp. from fat-water separators - includes mixing and sedimenting fat, further separating at specific temp. and filtering and vacuum-distilling |
| JP2000263080A (en) * | 1999-03-17 | 2000-09-26 | Kawasaki Steel Corp | Treatment method for organic-containing alkaline waste liquid |
| US20050131086A1 (en) * | 2002-06-18 | 2005-06-16 | Dancuart Kohler Luis P.F. | Method of purifying fischer-tropsch derived water |
| US20080023407A1 (en) * | 2003-12-17 | 2008-01-31 | Denis ANGELERI | Water Treatment Process |
| CN1654352A (en) * | 2005-01-06 | 2005-08-17 | 重庆大学 | System and method for urban sewage chemical-biologic composite deep phosphorous removal |
| CN1966428A (en) * | 2006-10-16 | 2007-05-23 | 西安长庆科技工程有限责任公司 | Gas field methanol sewage disposal process |
| CN101250017A (en) * | 2008-04-02 | 2008-08-27 | 总装备部工程设计研究总院 | Purification technique for methyl stannum mercaptide industrial sewage |
| CN101549938A (en) * | 2009-04-29 | 2009-10-07 | 浙江商达水务有限公司 | Method for treating waste water containing high concentration of organosilicon |
| CN102001794A (en) * | 2010-11-30 | 2011-04-06 | 华东理工大学 | Method for treating unsaturated polyester resin production wastewater |
| CN202390289U (en) * | 2011-12-21 | 2012-08-22 | 江阴明大化工有限公司 | Device for treating unsaturated polyester process wastewater efficiently |
| CN102976543A (en) * | 2012-12-18 | 2013-03-20 | 深圳市能源环保有限公司 | Garbage leachate disposal method and system |
| CN103482715A (en) * | 2013-09-16 | 2014-01-01 | 惠州Tcl环境科技有限公司 | High-concentration organic waste water evaporating and concentration processing method |
| CN103588356A (en) * | 2013-10-17 | 2014-02-19 | 东莞云水谣环保科技有限公司 | Combination system for treating landfill leachate and method for treating landfill leachate by using combination system |
| CN103601616A (en) * | 2013-11-20 | 2014-02-26 | 杭州上一环保技术有限公司 | Alcohol-water separation recycling method of fischer-tropsch synthesis reaction water |
| CN104609665A (en) * | 2015-01-21 | 2015-05-13 | 四川省环境保护科学研究院 | Glyphosate-producing wastewater treatment integration technology |
| CN204779248U (en) * | 2015-06-16 | 2015-11-18 | 大连广泰源环保科技有限公司 | A sewage treatment system for landfill leachate |
| CN204958664U (en) * | 2015-08-26 | 2016-01-13 | 合肥中盛水务发展有限公司 | Processing system of medicine waste water |
| CN105254141A (en) * | 2015-11-24 | 2016-01-20 | 广东先导稀材股份有限公司 | Treatment method and treatment system for high-concentration mixed salt organic wastewater |
| CN105366863A (en) * | 2015-11-24 | 2016-03-02 | 山东东岳氟硅材料有限公司 | High-efficient eco-friendly processing method for reducing COD in sewage |
| CN205556392U (en) * | 2016-03-24 | 2016-09-07 | 福建省三净环保科技有限公司 | Sewage treatment equipment |
Non-Patent Citations (2)
| Title |
|---|
| 张永胜等: "高浓度有机物废水治理实例分析", 《河南科技学院学报(自然科学版)》 * |
| 马承愚等: "农药生产废水处理设施改造工程设计", 《给水排水》 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201400628Y (en) | Down wastewater treatment system | |
| CN203065291U (en) | Closed cycle treatment system for paint-spraying wastewater | |
| CN108298741A (en) | A kind of oily wastewater electric flocculation high-level cleaner | |
| CN202881049U (en) | Buried type sewage treatment device | |
| CN107555600A (en) | A kind of sewage disposal system | |
| CN107585972A (en) | Grease processing waste water handling process and device | |
| CN205556392U (en) | Sewage treatment equipment | |
| CN201400629Y (en) | Floor processing wastewater treatment and recycling system | |
| CN105417862A (en) | Wastewater treatment system | |
| CN208949075U (en) | Novel anaerobic reactor | |
| CN207091248U (en) | A kind of Waste Water Treatment in Chinese medicine preparation | |
| CN106830574A (en) | A kind of New Type of Sewage Treatment System | |
| CN201400631Y (en) | Plastic cleaning wastewater treatment system | |
| CN208829505U (en) | After-treatment system of the Fine Chemistry Wastewater after MVR distills | |
| CN208732860U (en) | Sewage disposal system containing active dye printing | |
| CN207525100U (en) | A kind of drum type brake integrated sewage treating apparatus | |
| CN206089332U (en) | Sewage resource system up to standard is synthesized in multi -functional villages and small towns | |
| CN107226579A (en) | A kind of sewage disposal device | |
| CN108793597A (en) | A kind of higher suspension solid concentration stain disease reuse project method | |
| CN206384985U (en) | Breeding wastewater comprehensive purification system | |
| CN207713572U (en) | A kind of New Type of Sewage Treatment System | |
| CN106927621A (en) | A kind of sanitary sewage disposal detection means | |
| CN206828333U (en) | A kind of device for recycling breeding wastewater | |
| CN207811366U (en) | A kind of sewage disposal system | |
| CN206359399U (en) | Sewage disposal system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: No.889, East Second Ring Road, Anxi County, Quanzhou City, Fujian Province Applicant after: Fujian Zhongke Sanjing environmental protection Co.,Ltd. Address before: 362400, Quanzhou County, Fujian City, Chengxiang province Anxi Town Village Road Applicant before: FUJIAN SANJING ENVIRONMENTAL PROTECTION FACILITY & TECHNOLOGY Co.,Ltd. |
|
| CB02 | Change of applicant information | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20171003 |
|
| WD01 | Invention patent application deemed withdrawn after publication |