CN206089331U - Beer effluent disposal system - Google Patents
Beer effluent disposal system Download PDFInfo
- Publication number
- CN206089331U CN206089331U CN201620810763.7U CN201620810763U CN206089331U CN 206089331 U CN206089331 U CN 206089331U CN 201620810763 U CN201620810763 U CN 201620810763U CN 206089331 U CN206089331 U CN 206089331U
- Authority
- CN
- China
- Prior art keywords
- sludge
- pump
- pipeline
- beer
- acidification pool
- 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.)
- Active
Links
Landscapes
- Activated Sludge Processes (AREA)
Abstract
The utility model discloses a beer effluent disposal system, including grid, catch basin, water conservancy sieve, equalizing basin, hydrolysis -acidification pool, two -stage process contact oxidation tank, the elevator pump of catch basin in through the pump house is connected to the water conservancy plus sieve, the equalizing basin still is connected with an acid -base jar, still is provided with stealthily dirty pump of mud in hydrolysis -acidification pool and two -stage process contact oxidation tank, and mud stealthily dirty pump has a ji nijing through the tube coupling, and jinijing has a sludge tihckener through the tube coupling, and sludge tihckener has a desliming room through the tube coupling, hydrolysis -acidification pool includes pre -reaction district, dominant reaction district, still be provided with the dive mixer in the pre -reaction district, the dominant reaction district includes follows supreme mechanical stirring section and the aeration contact -segment that sets up in turn down, the mechanical stirring section includes agitating unit, the aeration contact -segment is provided with aeration equipment. This processing system simple structure has optimized the treatment process of beer waste water through this processing system, can compromise the minimizing of mud simultaneously and deal with.
Description
Technical field
The utility model belongs to Treatment of Beer Wastewater field, and in particular to a kind of Treatment of Beer Wastewater system.
Background technology
China is the first Beer Brewage big country in the world, and annual hundred million tons of brewing industry institute effluent about 4-5, beer waste water is rich
Organic wastewater containing intermediate concentrations such as carbohydrate, alcohols, biochemical is preferable, if in line be put in periphery natural water, can be to ring
Huge pollution is caused in border, therefore the effective process of beer waste water is a problem demanding prompt solution.
In processing procedure, each kiloton waste water about produces industry dirt of the 2-3 tons moisture content 80% or so to beer waste water
Mud, sludge treatment takes at 250-500 yuan/ton or so, therefore the minimizing of sludge advantageously reduces sludge treatment expense.
Beer waste water COD typically in 1000-4000mg/L or so, biochemical in 0.4-0.6 or so, handling process compared with into
Ripe, generally using methods such as Anaerobic Treatment, Aerobic Process for Treatment, anaerobism+aerobic combinations, but these group technologies are more in design
Focus on standard water discharge, often ignore the minimizing disposal for taking into account sludge.Therefore it is up to standard in guarantee Treatment of Beer Wastewater, while realize,
Sludge realizes minimizing, and such a Treatment of Beer Wastewater system has major economic value.
Utility model content
The utility model proposes a kind of Treatment of Beer Wastewater system, the processing system simple structure, by optimization hydrolysis acid
Change pond construction and the method for operation, two kinds of effects of minimizing of standard water discharge and sludge can be realized.
What the technical solution of the utility model was realized in：A kind of Treatment of Beer Wastewater system, it is characterised in that include
Grid, collecting-tank, hydraulic screen, regulating reservoir, hydrolysis acidification pool, the two sections of contact-oxidation pools being sequentially connected with by pipeline, collecting-tank
Top is provided with pump house, and collecting-tank is connected on hydraulic screen by the elevator pump in pump house, and it is sour that the regulating reservoir is also associated with one
Alkali tank, is additionally provided with sludge submersible sewage pump in hydrolysis acidification pool and two sections of contact-oxidation pools, and sludge submersible sewage pump is connected by pipeline
There is mud-collecting well, mud-collecting well is connected with sludge concentration tank by pipeline, and sludge concentration tank is connected with desliming room by pipeline, described de-
Mud room and sludge concentration tank are also connected on pump house by pipeline, and the hydrolysis acidification pool includes pre-reaction zone, main reaction region, institute
State pre-reaction zone to be connected by water hole with main reaction region, diving mixer, main reaction are additionally provided with the pre-reaction zone
Area includes mechanical agitation section and the aeration contact-segment being arranged alternately from bottom to up, and the mechanical agitation section includes agitating device, institute
State aeration contact-segment and be provided with aerator, sludge submersible sewage pump and filler are additionally provided with the main reaction region, the sludge is dived
By pipeline by sludge reflux to pre-reaction zone, the Treatment of Beer Wastewater system is controlled dirty pump by PLC system.
Further, the hydrolysis acidification pool is arranged in order for 3 or more than 3, while completing into water mixing, standing and sink
Form sediment and three steps of water outlet.
Further, described filler is netted spheroid, and ball is provided with netted spheroid.
The beneficial effects of the utility model are as follows：The processing system simple structure, by optimize hydrolysis acidification pool construction and
The method of operation, can realize taking into account two kinds of effects of minimizing of standard water discharge and sludge.
Description of the drawings
In order to be illustrated more clearly that the utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or the accompanying drawing to be used needed for description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, before creative labor is not paid
Put, can be with according to these other accompanying drawings of accompanying drawings acquisition.
Fig. 1 is Beer wastewater treatment technology flow chart；
Fig. 2 is the structural representation of hydrolysis acidification pool；
Fig. 3 is the structural representation of filler；
Fig. 4 is the structural representation of main reaction region.
In figure：1st, grid；2nd, collecting-tank；3rd, hydraulic screen；4th, regulating reservoir；5th, soda acid tank；6th, hydrolysis acidification pool；7th, two sections connect
Tactile oxidation pond；8th, pump house；9th, mud-collecting well；10th, sludge concentration tank；11st, desliming room；12nd, sludge submersible sewage pump；13rd, aeration contact
Section；14th, main reaction region；15th, pre-reaction zone；16th, filler；17th, aerator；18th, agitating device；19th, mechanical agitation section；20、
Ball；21st, diving mixer.
Specific embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of the utility model protection.
Referring to a kind of Treatment of Beer Wastewater system shown in Fig. 1 to Fig. 3, including the grid 1, collection that are sequentially connected with by pipeline
Pond 2, hydraulic screen 3, regulating reservoir 4,6, two sections of contact-oxidation pools 7 of hydrolysis acidification pool, the top of collecting-tank 2 is provided with pump house 8, catchments
Pond 2 is connected on hydraulic screen 3 by the elevator pump in pump house 8, and the regulating reservoir 4 is also associated with a soda acid tank 5, in hydrolysis acidification
Sludge submersible sewage pump 12 is additionally provided with pond 6 and two sections of contact-oxidation pools（It is not shown）, sludge submersible sewage pump 12 is connected with by pipeline
Mud-collecting well 9, mud-collecting well 9 is connected with sludge concentration tank 10 by pipeline, and sludge concentration tank 10 is connected with desliming room 11 by pipeline,
The desliming room 11 and sludge concentration tank 10 are also connected on pump house 8 by pipeline, and the hydrolysis acidification pool 6 includes pre-reaction zone
15th, main reaction region 14, the pre-reaction zone 15 is connected with main reaction region 14 by water hole, is also set in the pre-reaction zone 15
Diving mixer 21 is equipped with, main reaction region includes mechanical agitation section 19 and the aeration contact-segment 13 being arranged alternately from bottom to up, institute
Mechanical agitation section 19 is stated including agitating device 18, the aeration contact-segment 13 is provided with aerator 17, in the main reaction region
Sludge submersible sewage pump 12 and filler 16 are additionally provided with, the sludge submersible sewage pump 12 is connected in pre-reaction zone 15 by pipeline, should
Treatment of Beer Wastewater system is controlled by PLC system.
When in use process is as follows for the utility model, and the waste water in beer production is entered directly in grid 1,
Grid 1 is filtered large volume of suspension therein, and then the water Jing after grid maker process imports collecting-tank 2, catchments
The effect in pond 2 is to store and adjust beer waste water, it is ensured that biological treatment facility can obtain in one day and inflow and water
Matter, after collecting-tank 2 has been stored to enough waste water, due to being provided with pump house 8 below, elevator pump is by waste water in pump house 8
During hydraulic screen 3 will be pumped into, hydraulic screen 3 further filters the waste water in collecting-tank 2, by the suspension of wherein smaller size smaller
Remove, then waste water is flowed in regulating reservoir 4, and soda acid tank 5 is connected with regulating reservoir 4, adjusted the pH value of waste water by soda acid tank 5
6.5-7 or so is saved, after the pH value regulation of waste water is completed, elevator pump is again transported to waste water in hydrolysis acidification pool 6, hydrolysis
Acidification pool 6 is hydrolyzed acidifying to waste water, and particularly, waste water first carries out pre-reaction, the pre-reaction zone in pre-reaction zone 15
15 are provided with latent dirt mixer 21, the sludge that end is flowed back can be evenly mixed in waste water, when waste water enters into the reaction
After area, sludge can dissolved organic matter in quick adsorption sewage, complete the matrix Rapid Accumulation process of high load capacity.When pre- anti-
After should terminating, waste water enters into main reaction region 14 by intercommunicating pore, and the He of mechanical agitation section 19 is provided with main reaction region 14
Aeration contact-segment, forms anaerobism-and oxygen-anaerobism replaces, and in mechanical agitation section anaerobic hydrolysis-acidification reaction is can speed up, and is exposing
Sludge aerobic oxidation organic matter under simultaneous oxygen environment in gas contact-segment.After the completion of hydrolysis acidification, can efficiently by waste water
Larger molecular organicses are converted into small molecule, and wastewater effluent process is then carried out again, and waste water enters into two sections of contact-oxidation pools 7 and relays
It is continuous to carry out oxidation reaction, after oxidation reaction is completed, then discharged, excess sludge is flowed in mud-collecting well 9, is finally passed through again
Mud-collecting well 9 is entered in sludge concentration tank 10, and sludge concentration tank 10 is further concentrated sludge, and sewage therein is passed through
Pump house 8 is again fed to be processed again in collecting-tank, enters finally in desliming room 11 and carry out outward transport landfill.
Simultaneously sludge submersible sewage pump can be by the pre-reaction of a part of residual sludge reflux to hydrolytic tank in two sections of contact-oxidation pools
Area 15, be hydrolyzed again acidification reaction, after carrying out the reaction in one or more cycles, the quilt such as organic matter in sludge
Totally, yield is reduced microbial consumption.
Further, the hydrolysis acidification pool 6 is three or more and is arranged in order.The utility model is due to hydrolysis acidification
Pond 6 is for three or more and is arranged in order, and by becoming more meticulous to the regulation and control of beer waste water Hydrolysis Acidification efficiency is improved, and is divided into
Stirring hybrid reaction, quiescent setting, 3 continuous process of water outlet, three processes are simultaneously complete in three or more different ponds respectively
Into, successively complete to hydrolyze sequential process with continuous batch mode in same pond, process and realize continuous flow.I.e. in continuous hydrolysis,
At least always there is a pond in water inlet stirring mixing, a pond is in quiescent setting, and a pond is in out water state, such as A Chi Chu
In entering water state；B ponds intake prior to A ponds, and stirring is completed in precipitated form；C ponds intake prior to B ponds, and precipitation is completed, is in out
Water state.This mode relative to prior art, because Hydrolysis Acidification is completed in different ponds, it can be ensured that hydrolysis each stage
Required optimum reacting time, improves hydrolysis effect；And the hydrolytic tank of conventional method is adopted, it is to be separately provided a precipitation in hydrolytic tank
Pond, floor space is larger with investment, while Hydrolysis Acidification is more chaotic, stirring hybrid reaction, quiescent setting and water outlet are same
Shi Jinhang, so hydrolysis effect is bad；And the utility model stirs hybrid reaction, quiet by three steps of hydrolysis acidification pool, that is,
Only precipitation, water outlet is integrated, and using modularized design and expansion, is more beneficial for waste water treatment engineering built by separate periods and expansion
Build.
Further, described filler 16 is netted spheroid, and ball 20 is provided with netted spheroid.In order to strengthen with activity
Sludge is main body hydrolysis acidification ability and capacity of resisting impact load, adds suspension ball filler 16, and the filler 16 adopts double-layer ball
Body structure, outside is fishing net shaped spheroid, and inside is rotary-type spheroid, effectively in anaerobism, and oxygen and the microorganism such as aerobic attachment life
It is long.Floating-ball type filler 16 is adopted simultaneously, is conducive to operation later stage filler 16 to change and safeguard.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements made etc. should be included in the utility model
Protection domain within.
Claims (3)
1. a kind of Treatment of Beer Wastewater system, it is characterised in that include grid, collecting-tank, the waterpower being sequentially connected with by pipeline
Sieve, regulating reservoir, hydrolysis acidification pool, two sections of contact-oxidation pools, collecting-tank top is provided with pump house, and collecting-tank is by carrying in pump house
Rise pump to be connected on hydraulic screen, the regulating reservoir is also associated with a soda acid tank, in hydrolysis acidification pool and two sections of contact-oxidation pools
Sludge submersible sewage pump is additionally provided with, sludge submersible sewage pump is connected with mud-collecting well by pipeline, and it is dense that mud-collecting well is connected with sludge by pipeline
Contracting pond, sludge concentration tank is connected with desliming room by pipeline, and the desliming room and sludge concentration tank are also connected to pump by pipeline
Fang Shang, the hydrolysis acidification pool includes pre-reaction zone, main reaction region, and the pre-reaction zone and main reaction region are connected by water hole
It is logical, diving mixer is additionally provided with the pre-reaction zone, main reaction region includes the mechanical agitation section being arranged alternately from bottom to up
With aeration contact-segment, the mechanical agitation section includes agitating device, and the aeration contact-segment is provided with aerator, and the master is anti-
Answer and be additionally provided with area sludge submersible sewage pump and filler, the sludge submersible sewage pump is connected in pre-reaction zone by pipeline, the beer
Wine Waste Water Treatment is controlled by PLC system.
2. Treatment of Beer Wastewater system according to claim 1, it is characterised in that the hydrolysis acidification pool is 3 or 3
More than it is arranged in order, while completing into water mixing, staticly settling and three steps of water outlet.
3. Treatment of Beer Wastewater system according to claim 2, it is characterised in that described filler is netted spheroid, in net
Ball is provided with shape spheroid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620810763.7U CN206089331U (en) | 2016-07-28 | 2016-07-28 | Beer effluent disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620810763.7U CN206089331U (en) | 2016-07-28 | 2016-07-28 | Beer effluent disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206089331U true CN206089331U (en) | 2017-04-12 |
Family
ID=58467337
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620810763.7U Active CN206089331U (en) | 2016-07-28 | 2016-07-28 | Beer effluent disposal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206089331U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947097A (en) * | 2017-05-27 | 2018-12-07 | 宝山钢铁股份有限公司 | A kind for the treatment of method and apparatus of leveling precision waste water by ozone biochemistry coupling |
-
2016
- 2016-07-28 CN CN201620810763.7U patent/CN206089331U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947097A (en) * | 2017-05-27 | 2018-12-07 | 宝山钢铁股份有限公司 | A kind for the treatment of method and apparatus of leveling precision waste water by ozone biochemistry coupling |
| CN108947097B (en) * | 2017-05-27 | 2021-10-22 | 宝山钢铁股份有限公司 | Ozone biochemical coupling treatment method and device for leveling liquid wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103641272B (en) | High concentrated organic wastewater and percolate zero-discharge treatment system | |
| CN203683215U (en) | Reinforced-circulation efficient anaerobic bioreactor applicable to dyeing wastewater treatment | |
| CN203530082U (en) | Printing and dyeing wastewater treatment and recycling system | |
| CN103523916A (en) | Reinforced circulating efficient anaerobic bioreactor applicable to dyeing and finishing wastewater treatment | |
| CN103771655A (en) | Cellulose ethanol fermentation waste liquor treatment method | |
| CN105130031B (en) | A kind of low-power membrane ozone air-float integrated apparatus | |
| CN206089331U (en) | Beer effluent disposal system | |
| CN203820526U (en) | Aerobic pool for sewage treatment and sewage treatment device | |
| CN101597561A (en) | A kind of biogas-lift reinforced anaerobic reactor and application thereof | |
| CN100509659C (en) | Zero-discharging treatment method of regenerated waste water for paper making | |
| CN103755027B (en) | Composite circular biochemical film reclaimed water integral treatment equipment and process | |
| CN206089332U (en) | Sewage resource system up to standard is synthesized in multi -functional villages and small towns | |
| CN207193062U (en) | Efficient dephosphorization system | |
| CN201433210Y (en) | Methane lifting type intensified anaerobic reactor | |
| CN108341560A (en) | A kind of Small Town Wastewater treatment process based on anaerobism MBR technology | |
| CN211170336U (en) | Combined pressure aeration aerobic reaction device | |
| CN209537248U (en) | A kind of emergency landfill leachate treatment equipment | |
| CN203392982U (en) | High-concentration organic wastewater treatment device | |
| CN101891346A (en) | Discharge-reducing method for biologically treating chemical-mechanical pulping waste water | |
| CN206886768U (en) | It is a kind of that dyeing waste water is handled using electroosmose process and reclaims the device used | |
| CN205616722U (en) | High concentration printing and dyeing wastewater's treatment facility | |
| CN204356197U (en) | Modified form MSBR reactor | |
| CN204981502U (en) | Wash a meter sewage treatment system | |
| CN204474492U (en) | Polyester waste water treatment system | |
| CN204897653U (en) | Rubber effluent disposal system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |