CN202449958U - Rubber waste water treatment system - Google Patents
Rubber waste water treatment system Download PDFInfo
- Publication number
- CN202449958U CN202449958U CN2012200135132U CN201220013513U CN202449958U CN 202449958 U CN202449958 U CN 202449958U CN 2012200135132 U CN2012200135132 U CN 2012200135132U CN 201220013513 U CN201220013513 U CN 201220013513U CN 202449958 U CN202449958 U CN 202449958U
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- tank
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- mbr
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- pump
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
Abstract
The utility model provides a rubber waste water treatment system. Waste water is fed into a water collecting tank, the water collecting tank is connected with an adjusting tank through a lifting pump, the adjusting tank is connected with an iron carbon tower through a centrifugal pump, an outlet of the iron carbon tower is connected with a neutralization sedimentation tank through a waste water pipeline of the iron carbon tower, an inclined pipe sedimentation tank is arranged in the neutralization sedimentation tank which is connected with a facultative anaerobic hydrolyzing tank through a waster water pipeline of the neutralization sedimentation tank, the facultative anaerobic hydrolyzing tank is connected with a membrane biological reactor (MBR) tank through a waster water pipeline of the facultative anaerobic hydrolyzing tank, the MBR tank is connected with a monitoring well through a suction pump, a sludge pipe of the inclined pipe sedimentation tank and a sludge pipe of the MBR tank are converged and then connected with a sludge treatment system through a screw pump, and the sludge treatment system is communicated with the water collecting tank through a water pipe.
Description
Technical field
The utility model relates to a kind of Sewage treatment systems, particularly a kind of Rubber Industrial Wastewater treatment system.
Background technology
Urban sewage discharge has been the primary pollution source of China's municipal water at present, and municipal sewage treatment is the most important thing of urban water conservation at present and in the future and Urban Water Environment protection work.Municipal effluent comprises sewage and industrial sewage, and wherein the industrial sewage kind is a lot, to different sources, needs different processing.
Complicated component in cis-1,4-polybutadiene rubber waste water and the sbr wastewater, organic content is high, and it is more to contain hardly degraded organic substance, and BOD
5/ CODcr value is on the low side, and directly intractability is bigger.
Summary of the invention
The purpose of the utility model provides a kind of Rubber Industrial Wastewater treatment system, and sewage treatment equipment is huge in the solution prior art, and processing efficiency is low, and because the more difficult isolating technical problem of complicated component.
The utility model mainly is able to solve through following technical scheme:
A kind of Rubber Industrial Wastewater treatment system; The water collecting basin that feeds waste water connects equalizing tank via lift pump, and equalizing tank connects iron carbon tower via impeller pump, and the outlet of iron carbon tower connects the neutralization precipitation pond via iron carbon tower waste pipe; Neutralization precipitation is provided with tube settler in the pond; The neutralization precipitation pond connects the concurrent oxidation and aquoiysis pond via neutralization precipitation pond waste pipe, and the concurrent oxidation and aquoiysis pond connects the MBR pond via concurrent oxidation and aquoiysis pond waste pipe, and the MBR pond connects monitor well via suction pump.
Described tube settler sludge pipe converges with MBR pond sludge pipe after be connected sludge treating system by spiral pump, and sludge treating system is communicated with water collecting basin via water pipe.
Described water collecting basin comprises grille well and oil trap, and grille well is via water pump, valve and pipe connection oil trap.
Described concurrent oxidation and aquoiysis pond and MBR pond all are equipped with micro-hole aerator and reinforced polyvinyl chloridepipe aerating system.
Described sludge treating system is equipped with plate-and-frame filter press.
Here, MBR is the English abbreviation of membrane bioreactor (Membrane Bio-Reactor)
The utility model is applicable to most of Rubber Industrial Wastewater processing, and its treatment unit is simple and easy to control, and it is lower that treating processes articulation efficiency, treatment process are compared the additive method energy consumption, can be described as energy-conservation.
Description of drawings
Fig. 1 is the system architecture synoptic diagram of the utility model.
Embodiment
Below in conjunction with accompanying drawing and instance the present invention is done further description.
As shown in Figure 1; Waste water feeds water collecting basin and is promoted to equalizing tank via lift pump, and equalizing tank is promoted to iron carbon tower via impeller pump, and the outlet of iron carbon tower connects the neutralization precipitation pond via waste pipe; Neutralization precipitation is provided with tube settler in the pond; The neutralization precipitation pond connects the concurrent oxidation and aquoiysis pond via waste pipe, and the concurrent oxidation and aquoiysis pond connects the MBR pond via waste pipe, and the MBR pond connects monitor well via suction pump; Described tube settler all is connected plate-and-frame filter press via spiral pump with the MBR pond, and plate-and-frame filter press is communicated with water collecting basin via water pipe.
Described water collecting basin comprises grille well and oil trap; Grille well is connected oil trap via water pump with valve pipe; Described concurrent oxidation and aquoiysis pond and MBR pond all are equipped with micro-hole aerator and reinforced polyvinyl chloridepipe aerating system, and described sludge treating system setting is equipped with plate-and-frame filter press.
1. water collecting basin: flow into water collecting basin after on-site waste water compiles, advance before the water collecting basin, remove the large particulate matter in the waste water, with anti-clogging plug water pump and valve pipe earlier through grille well.Oil trap is to remove the grease that floats on the surface.Be promoted to equalizing tank by lift pump then.
2. equalizing tank: equalizing tank function homogeneous, equal amounts.In equalizing tank, adding dilute sulphuric acid regulates pH value and is promoted to iron carbon tower by corrosion resisting centrifugal pump to 2-3..
3. iron carbon tower: mix, the PH2-3 Rubber Industrial Wastewater is transported to iron carbon tower.Filler is made up of plane iron flower (being the waste material that lathe turning is got off) and grain active carbon in the iron carbon tower.Wherein the plane iron flower is 5: 1 (w/w) with the input ratio of grain active carbon. drop into successively in the tower, make the two distribution even as far as possible.Waste water stopped 12 hours in iron carbon tower, noted plane iron flower oxidation situation in the tower.Often add the plane iron flower to guarantee its iron carbon rational proportion.
4. neutralization precipitation pond: add Ca (OH) in the water outlet of iron carbon tower
2Carry out the PH adjustment.First lattice add Ca (OH) automatically through PH on-line monitoring appearance in neutralization tank
2, control PH:7.5-8.5, adopt mechanical stirring to mix.Add flocculation agent PAM in second lattice, make the small-particle coacervating large particle, accelerate sludge settling.
Tube settler precipitates suspended substance (SS).Tube settler bottom mud is pressed in the plate-and-frame filter press with spiral pump and dewaters.Inclined tube is answered periodic flushing in the tube settler, prevents that top suspended substance from accumulating too much its function that influences.
5. concurrent oxidation and aquoiysis pond: because Rubber Industrial Wastewater B/C ratio, so waste water makes through the concurrent oxidation and aquoiysis pond that the macromolecular organic pollutant of difficult degradation is hydrolyzed to micromolecular organic pollutant in the waste water, thereby improves the biodegradability of waste water.Semi soft packing, aerating system 1 cover, (KBB micro-hole aerator, UPVC pipe) are installed, intermittent aeration, control dissolved oxygen≤0.5mg/l in the concurrent oxidation and aquoiysis pond.
6.MBR pond: MBR is biologic treating technique a kind of novel, sewage disposal technology efficiently that combines with membrane separation technique.It is mainly by bio-reactor and the combination of membrane module two unit equipments.Micro-hole aerator is installed in the pond, and UPVC manages aerating system.The control dissolved oxygen is at 2-5mg/l.
The MBR gordian technique:
Therefore A. the membrane sepn process does not undergo phase transition with the data by MoM and MEI energy consumption lowlyer, claims power-saving technology again.
B. the membrane sepn process is carried out at normal temperatures, thereby is particularly suitable for the processing of heat-sensitive material.Membrane sepn has unique flexibility in all kinds of waste water treatments.
C. membrane separation technique is not only applicable to the separating of organism and inorganics, biologically separates to particulate with virus, bacterium, but also is applicable to the separation of many singular solution systems.Like separating of macromole in the solution and inorganic salt, the separation of some azeotropes or the system that closely boils etc., and the latter usually is helpless with conventional distillating method.
D. the membrane separation process tripping device is simple, processing ease and easy to control.Working temperature near room temperature, is convenient to maintenance management again, and separation efficiency is high, and safety is high.As a kind of novel water treatment method, compare with conventional water treatment method, it is small and exquisite to have facility compact, and processing efficiency is high, realizes automated operation easily, and floor space is little, can frequent starting or out-of-work characteristic, very flexibly.
E. the high performance membrane integrated technology constantly develops, price is fallen greatly, impel the application of membrane separation technology scope extremely extensive, water reuse field in particularly being applied to.For the big country of such one 1,300,000,000 population of China, utilize membrane separation technique to realize the reuse of waste water such as sewage, in a sense, will alleviate available water scarcity degree.The embrane method water technology will become the gordian technique of water treatment in 21 century, and it will be the revolution of water treatment.
7. sludge treating system:
Tube settler mud and unnecessary biochemical sludge are delivered to plate-and-frame filter press through spiral pump, and clear water is back to water collecting basin after the press filtration, and the dewatered sludge outward transport is disposed after the press filtration.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012200135132U CN202449958U (en) | 2012-01-13 | 2012-01-13 | Rubber waste water treatment system |
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CN2012200135132U CN202449958U (en) | 2012-01-13 | 2012-01-13 | Rubber waste water treatment system |
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CN202449958U true CN202449958U (en) | 2012-09-26 |
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CN2012200135132U Expired - Fee Related CN202449958U (en) | 2012-01-13 | 2012-01-13 | Rubber waste water treatment system |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108439733A (en) * | 2018-06-11 | 2018-08-24 | 淄博职业学院 | A kind of petrochemical effluent comprehensive purifying equipment and its application method |
CN109626757A (en) * | 2019-01-29 | 2019-04-16 | 中环清源(北京)科技有限公司 | A kind of method of light electrolysis-MBR coupling technique treatment of laboratory waste water |
CN113943088A (en) * | 2021-11-19 | 2022-01-18 | 浙江天地环保科技股份有限公司 | A zero-discharge treatment system and method for SCR denitration catalyst regeneration wastewater |
-
2012
- 2012-01-13 CN CN2012200135132U patent/CN202449958U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108439733A (en) * | 2018-06-11 | 2018-08-24 | 淄博职业学院 | A kind of petrochemical effluent comprehensive purifying equipment and its application method |
CN109626757A (en) * | 2019-01-29 | 2019-04-16 | 中环清源(北京)科技有限公司 | A kind of method of light electrolysis-MBR coupling technique treatment of laboratory waste water |
CN113943088A (en) * | 2021-11-19 | 2022-01-18 | 浙江天地环保科技股份有限公司 | A zero-discharge treatment system and method for SCR denitration catalyst regeneration wastewater |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120926 Termination date: 20160113 |