CN209081685U - A kind of monkshood factory processing waste water processing unit - Google Patents
A kind of monkshood factory processing waste water processing unit Download PDFInfo
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- CN209081685U CN209081685U CN201821921196.8U CN201821921196U CN209081685U CN 209081685 U CN209081685 U CN 209081685U CN 201821921196 U CN201821921196 U CN 201821921196U CN 209081685 U CN209081685 U CN 209081685U
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- pipe
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- sedimentation basin
- monkshood
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Abstract
The utility model discloses a kind of monkshood factory processing waste water processing units, it is related to technical field of sewage treatment equipment, solves monkshood factory processing waste water complicated component, conventional sewage processing equipment is difficult to the problem of being effectively treated, the utility model includes the acidification conditioning tank set gradually, upflow anaerobic sludge blanket process, aeration tank, sedimentation basin and clear water reserviors, immersible pump a is provided in acidification conditioning tank, immersible pump a is connected to the bottom inside upflow anaerobic sludge blanket process by water-supply-pipe a, upflow anaerobic sludge blanket process top outer wall is provided with the water-supply-pipe b of connection aeration bottom of pond portion, aerator is provided in aeration tank, aeration tank top pool wall is provided with the water-supply-pipe c of connection sedimentation basin, sedimentation basin connects clear water reserviors by overflow mechanism, immersible pump b is provided in clear water reserviors, immersible pump b connects city planting ductwork by drainpipe.
Description
Technical field
The utility model relates to technical field of sewage treatment equipment, at a kind of monkshood factory processing waste water
Manage device.
Background technique
Environmental pollution has become today's society urgent problem to be solved, and the pollution of water resource be in problem of environmental pollution most
Important a part.Monkshood processing waste water main source has, cleaning silt generate waste water, slice generate water, drift piece waste water,
Boil the waste water of monkshood.The main component of the waste water is a large amount of silt, calcium chloride, starch, protein, fat, suspended matter etc..If
The sewage that project generates is directly discharged into the content that will lead to the organic matter in natural water in local natural water without processing
Greatly increase, lead to natural water eutrophication, bacterium mass propagation consumes the oxygen in water body, leads to aquatic animal anoxic
And there is the phenomenon that mortality, it is finally that water body blackening is fouled, the short time is difficult to restore.
Existing conventional sewage processing equipment is difficult to cope with the so complicated sewage of ingredient.
Utility model content
The purpose of this utility model is that: in order to solve monkshood factory processing waste water complicated component, conventional sewage processing equipment
It is difficult to the problem of being effectively treated, the utility model provides a kind of monkshood factory processing waste water processing unit
The utility model specifically uses following technical scheme to achieve the goals above:
A kind of monkshood factory processing waste water processing unit, including set gradually acidification conditioning tank, upflow anaerobic sludge blanket process,
Aeration tank, sedimentation basin and clear water reserviors are acidified in conditioning tank and are provided with immersible pump a, and immersible pump a passes through water-supply-pipe a connection up-flow
The bottom of the anaerobic mud bed inside of formula, upflow anaerobic sludge blanket process top outer wall are provided with the water-supply-pipe b of connection aeration bottom of pond portion,
Aerator is provided in aeration tank, aeration tank top pool wall is provided with the water-supply-pipe c of connection sedimentation basin, and sedimentation basin passes through overflow
Device connects clear water reserviors, is provided with immersible pump b in clear water reserviors, immersible pump b connects city planting ductwork by drainpipe.
It is further improved, is divided into inhalant region, reaction zone and Disengagement zone from the bottom to top inside upflow anaerobic sludge blanket process, intake
Bottom at area is inverted cone shape, and Disengagement zone is provided with three phase separator, and three phase separator includes fixed frame, and fixed frame lower surface is set
There is the baffle of several tapers, water-supply-pipe b is arranged in Disengagement zone.
It is further improved, aerator includes the aeration tube that aeration tank bottom is arranged in, and aeration tube is connected by air hose
External air compressor is provided with several aeration spray heads on aeration tube, is provided with flow-disturbing layer above aeration tube in aeration tank.
It being further improved, sedimentation basin center vertical is provided with water inlet pipe, and water inlet pipe top connects the end water-supply-pipe c, into
Water pipe bottom end is provided with the flow-stopping plate of taper, and sedimentation basin bottom of pond is inverted cone shape, and being horizontally disposed with up and down in sedimentation basin has two layers of filtering
Layer.
It is further improved, overflow mechanism includes the L-shaped overflow plate being arranged at the top of sedimentation basin at pool wall, overflow plate and heavy
It is overflow launder between the pool wall of shallow lake pond, the side pool wall at overflow launder connects clear water reserviors bottom of pond by overflow pipe.
It is further improved, is provided with chemical feed pipe in clear water reserviors, the dehydrating agent storage tank outside chemical feed pipe connection is set on chemical feed pipe
It is equipped with flowmeter and delivery pump.
It is further improved, upflow anaerobic sludge blanket process and precipitating bottom of pond portion are provided with sludge pipe, and sludge pipe connection is external
Sludge-tank.
The beneficial effects of the utility model are as follows:
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Appended drawing reference: 1- is acidified conditioning tank, 2- immersible pump a, 3- water-supply-pipe a, 4- reaction zone, 5- up-flow anaerobic sludge
Bed, 6- fixed frame, 7- baffle, the Disengagement zone 8-, 9- air compressor, 10- dehydrating agent storage tank, 11- flowmeter, 12- delivery pump,
13- water-supply-pipe b, 14- air hose, 15- chemical feed pipe, 16- flow-disturbing layer, 17- aeration spray head, 18- aeration tube, the aeration tank 19-, 20-
Overflow plate, 21- water-supply-pipe c, 22- overflow launder, 23- overflow pipe, 24- clear water reserviors, 25- drainpipe, 26- immersible pump b, 27- filtering
Layer, 28- water inlet pipe, 29- flow-stopping plate, 30- inhalant region, 31- sludge pipe, 32- sludge-tank, 33- sedimentation basin.
Specific embodiment
In order to which those skilled in the art better understand the utility model, with reference to the accompanying drawing with following embodiment to this
Utility model is described in further detail.
Embodiment 1
A kind of monkshood factory processing waste water processing unit, including acidification conditioning tank 1, the upflow anaerobic sludge blanket process set gradually
5, aeration tank 19, sedimentation basin 33 and clear water reserviors 24 are acidified in conditioning tank 1 and are provided with immersible pump a2, and immersible pump a2 passes through water delivery
Pipe a3 is connected to the bottom inside upflow anaerobic sludge blanket process 5, and 5 top outer wall of upflow anaerobic sludge blanket process is provided with connection aeration tank
The water-supply-pipe b13 of 19 bottoms, aerator is provided in aeration tank 19, and 19 top pool wall of aeration tank is provided with connection sedimentation basin 33
Water-supply-pipe c21, sedimentation basin 33 connects clear water reserviors 24 by overflow mechanism, is provided with immersible pump b26, immersible pump in clear water reserviors 24
B26 connects city planting ductwork by drainpipe 25.
According to specific examining report:
Slice, the water quality for cleaning silt are as follows:
| pH | COD | BOD | SS | Oils | TDS |
| 6~9 | 3850mg/L | 1260mg/L | 48600mg/L | 45mg/L | 3760mg/L |
Drift piece, boiling monkshood waste water quality are as follows:
| pH | COD | BOD | SS | Oils | Total salt quantity |
| 6~9 | 39662mg/L | > 6000mg/L | 650mg/L | 65mg/L | 33400mg/L |
It is discharged into city planting ductwork, executes " integrated wastewater discharge standard " grade III Standard:
| pH | COD | BOD5 | SS | Coloration | Ammonia nitrogen |
| 6~9 | ≤500mg/L | ≤300mg/L | ≤70mg/L | ≤400 | / |
It is discharged into surface water body, executes " Chinese medicine class pharmaceuticals industry pollution discharge standard " primary standard:
| pH | COD | BOD5 | SS | Coloration | Ammonia nitrogen |
| 6~9 | ≤100mg/L | ≤20mg/L | ≤50mg/L | ≤50 | ≤8 |
The dissolvability solid amount (TDS) in sewage by testing identical items is sometimes more than 10000mg/L, when super
Need artificial addition tap water that can carry out biochemical treatment when being diluted to 6000mg/L or less when crossing 10000mg/L.After dilution
Waste water passes through test, and the BOD/COD > 0.3 in sewage, therefore, sewage can use biochemical treatment.
Though sewage can cannot reach the organic matter in high load capacity degradation sewage with biochemical treatment, common anaerobic pond
Purpose needs to select more efficient Anaerobic Treatment facility, therefore, selects upflow anaerobic sludge blanket process (UASB) more appropriate.
UASB is the abbreviation of upflow anaerobic sludge blanket process, and the operation of high load capacity is capable of by debugging, and treatment effeciency is much big
In common anaerobic pond.The facility is broadly divided into three parts, inhalant region 30, reaction zone 4, Disengagement zone 8.Inhalant region 30 it is main
Component is water distributor, the water distributor mainly uniform laying and device bottom by sewage, and forms uniform ascending current pair
Top reaction zone 4 forms hydraulic mixing.
Reaction zone 4 is mainly the stop place of anaerobic bacteria, removes the main region of organic matter, UASB debug successfully after at this
Region forms the good floc sludge of a large amount of settling properties, and there are a large amount of anaerobic bacteria in the region, sewage passes through the region
When, anaerobic bacteria sufficiently decomposes the organic matter in sewage, and generates biogas, and the organic concentration in sewage reduces, the gas of generation
Body can also form faint stirring action to sewage.Floc sludge ascends into 8 domain of Disengagement zone with water flow.
Disengagement zone 8 is mainly three phase separator, which is separated mainly for the gas, liquid, solid body in sewage.Rise
Water flow in floc sludge release gas after back sink reaction zone 4 under the effect of gravity, water flow enter overflow weir outflow UASB into
Enter next treatment process.The top that biogas enters three separators enters water sealed tank by gas-guide tube and either discharges.
Though common anaerobic pond can degradation of organic substances volume is too big, and handle and meet much smaller than UASB, because
This, handling the waste water leading portion, to be designed as UASB more reasonable.
Concentration by the organic matter of sewage after UASB is still higher, therefore, it is necessary to which water flow, which enters, overflows using subsequent processing
Stream weir flow enter aeration tank 19 carry out Air Exposure, further remove the organic matter in anhydrous, then the sewage after Air Exposure into
Enter in sedimentation basin 33, precipitated, supernatant liquor is discharged into municipal pipeline through clear water reserviors 24.
If sewage is directly discharged into surface water body, electric flocculation device need to be added in above-mentioned apparatus end and set with ozone decolorization
It is standby.
In the present apparatus, acidification conditioning tank can be effectively acidified sewage, the biodegradability energy of lifting sewage, sewage
Effect by passing through sewage pump after hydrolysis acidification, which enters, carries out anaerobic reaction in UASB, under the action of anaerobic bacteria flora
The organic matter in sewage is decomposed, then sewage enters back into intermediate pool, subsequently into being handled in aerobic tank, subsequently into heavy
In the pond of shallow lake, the aerobic sludge in sewage is removed, into clear water reserviors, is then acted on again by filter, is removed outstanding in sewage
Floating object, from qualified discharge.
Embodiment 2
The present embodiment is to improve on the basis of embodiment 1:
It is divided into inhalant region 30, reaction zone 4 and Disengagement zone 8 inside upflow anaerobic sludge blanket process 5 from the bottom to top, at inhalant region 30
Bottom be inverted cone shape, Disengagement zone 8 is provided with three phase separator, and three phase separator includes fixed frame 6, and 6 lower surface of fixed frame is set
There is the baffle 7 of several tapers, water-supply-pipe b13 is arranged in Disengagement zone 8.
Embodiment 3
The present embodiment is to improve on the basis of embodiment 1:
Aerator includes the aeration tube 18 that 19 bottom of pond of aeration tank is arranged in, and aeration tube 18 connects outside by air hose 14
Air compressor, be provided with several aeration spray heads 17 on aeration tube 18, be arranged above aeration tube 18 in aeration tank 19 and thanks for your hospitality
Fluid layer 16.
Embodiment 4
The present embodiment is to improve on the basis of embodiment 1:
33 center vertical of sedimentation basin is provided with water inlet pipe 28, and 28 top of water inlet pipe connects the end water-supply-pipe c21, water inlet pipe
28 bottom ends are provided with the flow-stopping plate 29 of taper, and 33 bottom of pond of sedimentation basin is inverted cone shape, and being horizontally disposed with up and down in sedimentation basin 33 has two layers
Filter layer 27.
Embodiment 5
The present embodiment is improved on the basis of above embodiments:
Overflow mechanism includes the L-shaped overflow plate 20 being arranged at 33 top pool wall of sedimentation basin, overflow plate 20 and sedimentation basin
It is overflow launder 22 between 33 pool walls, the side pool wall at overflow launder 22 connects 24 bottom of pond of clear water reserviors by overflow pipe 23.
Embodiment 6
The present embodiment is improved on the basis of above embodiments:
Chemical feed pipe 15 is provided in clear water reserviors 24, chemical feed pipe 15 connects external dehydrating agent storage tank 10, sets on chemical feed pipe 15
It is equipped with flowmeter 11 and delivery pump 12.
Embodiment 7
The present embodiment is improved on the basis of above embodiments:
Upflow anaerobic sludge blanket process 5 and 33 bottom of sedimentation basin are provided with sludge pipe 31, and sludge pipe 31 connects external dirt
Mud sump 32.
The above, the only preferred embodiment of the utility model, are not intended to limit the utility model, the utility model
Scope of patent protection be subject to claims, it is equivalent made by all specifications and accompanying drawing content with the utility model
Structure change similarly should be included in the protection scope of the utility model.
Claims (7)
1. a kind of monkshood factory processing waste water processing unit, which is characterized in that including acidification conditioning tank (1), the up-flow set gradually
Formula anaerobic mud bed (5), aeration tank (19), sedimentation basin (33) and clear water reserviors (24) are acidified in conditioning tank (1) and are provided with diving
Pump a(2), immersible pump a(2) pass through water-supply-pipe a(3) and the internal bottom of connection upflow anaerobic sludge blanket process (5), up-flow anaerobism dirt
Mud bed (5) top outer wall is provided with the water-supply-pipe b(13 of connection aeration tank (19) bottom), aeration dress is provided in aeration tank (19)
Set, aeration tank (19) top pool wall is provided with the water-supply-pipe c(21 of connection sedimentation basin (33)), sedimentation basin (33) passes through overflow mechanism
Connect clear water reserviors (24), clear water reserviors are provided with immersible pump b(26 in (24)), immersible pump b(26) pass through drainpipe (25) connection city
Political affairs pipe network.
2. monkshood factory processing waste water processing unit according to claim 1, it is characterised in that: upflow anaerobic sludge blanket process
(5) internal to be divided into inhalant region (30), reaction zone (4) and Disengagement zone (8) from the bottom to top, the bottom at inhalant region (30) is back taper
Shape, Disengagement zone (8) are provided with three phase separator, and three phase separator includes fixed frame (6), and fixed frame (6) lower surface is equipped with several
The baffle (7) of taper, water-supply-pipe b(13) it is arranged in Disengagement zone (8).
3. monkshood factory processing waste water processing unit according to claim 1, it is characterised in that: aerator includes that setting exists
The aeration tube (18) of aeration tank (19) bottom of pond, aeration tube (18) pass through the air compressor outside air hose (14) connection, aeration
It is provided with several aeration spray heads (17) on pipe (18), is provided with flow-disturbing layer (16) above aeration tube (18) in aeration tank (19).
4. monkshood factory processing waste water processing unit according to claim 1, it is characterised in that: sedimentation basin (33) center vertical
It is provided with water inlet pipe (28), water inlet pipe (28) top connects water-supply-pipe c(21) end, water inlet pipe (28) bottom end is provided with taper
Flow-stopping plate (29), sedimentation basin (33) bottom of pond are inverted cone shape, and being horizontally disposed with up and down in sedimentation basin (33) has two filter layers (27).
5. monkshood factory processing waste water processing unit according to claim 1 to 4, it is characterised in that: overflow mechanism includes
L-shaped overflow plate (20) at the pool wall of sedimentation basin (33) top is set, is between overflow plate (20) and sedimentation basin (33) pool wall
Overflow launder (22), the side pool wall at overflow launder (22) connect clear water reserviors (24) bottom of pond by overflow pipe (23).
6. monkshood factory processing waste water processing unit according to claim 1 to 4, it is characterised in that: in clear water reserviors (24)
It is provided with chemical feed pipe (15), the dehydrating agent storage tank (10) outside chemical feed pipe (15) connection, chemical feed pipe is provided with flowmeter on (15)
(11) with delivery pump (12).
7. monkshood factory processing waste water processing unit according to claim 1 to 4, it is characterised in that: up-flow anaerobism is dirty
Mud bed (5) and sedimentation basin (33) bottom are provided with sludge pipe (31), the sludge-tank (32) outside sludge pipe (31) connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821921196.8U CN209081685U (en) | 2018-11-21 | 2018-11-21 | A kind of monkshood factory processing waste water processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821921196.8U CN209081685U (en) | 2018-11-21 | 2018-11-21 | A kind of monkshood factory processing waste water processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209081685U true CN209081685U (en) | 2019-07-09 |
Family
ID=67125139
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821921196.8U Expired - Fee Related CN209081685U (en) | 2018-11-21 | 2018-11-21 | A kind of monkshood factory processing waste water processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209081685U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110255696A (en) * | 2019-07-23 | 2019-09-20 | 大连民族大学 | A kind of system using remaining alkali Heat Treatment purified cotton black liquor |
-
2018
- 2018-11-21 CN CN201821921196.8U patent/CN209081685U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110255696A (en) * | 2019-07-23 | 2019-09-20 | 大连民族大学 | A kind of system using remaining alkali Heat Treatment purified cotton black liquor |
| CN110255696B (en) * | 2019-07-23 | 2022-05-10 | 大连民族大学 | System for utilize surplus alkali waste heat treatment refined cotton black liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190709 Termination date: 20201121 |