CN203112546U - Continuous adsorption system of sewage treatment process - Google Patents
Continuous adsorption system of sewage treatment process Download PDFInfo
- Publication number
- CN203112546U CN203112546U CN 201320061065 CN201320061065U CN203112546U CN 203112546 U CN203112546 U CN 203112546U CN 201320061065 CN201320061065 CN 201320061065 CN 201320061065 U CN201320061065 U CN 201320061065U CN 203112546 U CN203112546 U CN 203112546U
- Authority
- CN
- China
- Prior art keywords
- level
- absorption
- water
- backwash
- secondary absorption
- 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.)
- Withdrawn - After Issue
Links
Images
Abstract
A continuous adsorption system of a sewage treatment process comprises a primary adsorption device and a secondary adsorption device connected in series, wherein a secondary adsorption discharge pipe of the secondary adsorption device is connected onto a primary adsorbent guide cylinder (40) through a discharge connection pipe (30); a primary absorption water outlet pipe (31) is connected onto a secondary absorption water inlet pipe (16); and effluent discharging of the primary adsorption device can directly enter the secondary adsorption device for adsorption and also can enter the secondary adsorption device after being treated by other treatment processes. At the same time, new adsorbent can be added to the secondary adsorption device, the adsorbent saturated through secondary adsorption is lifted to the primary adsorption device for continuous use as the adsorbent, so that the adsorbent is saved; and the operation is easy, and the maintenance is convenient.
Description
Technical field
The utility model relates to the adsorption system in a kind of sewage treatment process.
Background technology
Absorption method is mainly used in removing the micropollutant in the water, should scope comprise removal of decolouring, deodorizing, various dissolved organic matters etc.Absorption method has applied widely, and treatment effect is good, characteristics such as recyclable useful material.
Traditional adsorption system is when adsorption bed needs backwash, and adsorption system can not be intake, and can only treat to return to adsorbed state after backwash is finished.
Traditional adsorption system needs to change sorbent material after absorption is saturated, when changing sorbent material, the adsorption system cisco unity malfunction could works better after the replacing sorbent material is finished.
Summary of the invention
Problem to be solved in the utility model is to overcome the deficiencies in the prior art; the working order that must shut down when overcoming traditional adsorption system when backwash and changing sorbent material; designed the continuous adsorption system of the utility model sewage treatment process; under the prerequisite that guarantees normal water inlet, water outlet; can carry out backwash operation; novel sorbents can be added automatically, saturated sorbent material can be drawn off automatically.Add novel sorbents, unload sorbent material automatically and all need not artificial loading and unloading.
Concrete scheme of the present utility model is: comprise the one-level adsorption unit and the secondary absorption device that connect with the series connection form;
Described one-level adsorption unit comprises one-level cylindrical shell, one-level water inlet cloth water unit, one-level air lift unit, one-level backwash unit, one-level feed unit, one-level adsorption bed, one-level water unit, described one-level water inlet cloth water unit comprises one-level absorption water inlet pipe, the one-level absorption water inlet pipe bottom one-level absorption water distribution awl of ining succession mutually arranges one-level absorption water distribution board on the one-level absorption water distribution awl; Described one-level air lift unit comprises that the one-level that is arranged on one-level cylindrical shell bottom is adsorbed airlift pump and coupled one-level is adsorbed the airlift pump inlet pipe, one-level is adsorbed the airlift pump inlet pipe and is picked out outside the one-level cylindrical shell, and one-level absorption air lift pump discharge connects one-level absorption discharge nozzle saturated sorbent material is carried from one-level cylindrical shell bottom to the one-level absorption drainage conduit of installing top; Described one-level backwash unit comprises one-level absorption backwash inlet pipe, one-level absorption backwash gas distribution pipe, one-level absorption backwash water shoot and one-level absorption backwash water discharge valve; Described one-level feed unit comprises the discharging pipe connecting, is nested in one-level sorbent material guide shell and one-level absorption cloth awl on the one-level absorption discharge nozzle; Described one-level water unit comprises one-level absorption effluent weir and the one-level absorption effluent pipe that is arranged on cylindrical shell top;
Described secondary absorption device comprises secondary cylindrical shell, secondary water inlet cloth water unit, secondary air lift unit, secondary backwash unit, secondary feed unit, secondary absorption bed, secondary effluent unit, described secondary water inlet cloth water unit comprises the secondary absorption water inlet pipe, in succession mutually secondary absorption water distribution awl of secondary absorption water inlet pipe bottom arranges the secondary absorption water distribution board on the secondary absorption water distribution awl; Described secondary air lift unit comprises the secondary absorption airlift pump that is arranged on secondary cylindrical shell bottom and coupled secondary absorption airlift pump inlet pipe, secondary absorption airlift pump inlet pipe picks out outside the secondary cylindrical shell, and the outlet of secondary absorption airlift pump connects the secondary absorption discharge nozzle saturated sorbent material is carried to the discharging pipe connecting on device top from secondary cylindrical shell bottom; Described secondary backwash unit comprises secondary absorption backwash inlet pipe, secondary absorption backwash gas distribution pipe, secondary absorption backwash water vent pipe and secondary absorption backwash water discharge valve; Described secondary feed unit comprises new hopper, virgin material conveying reducing motor, virgin material conveying axis, is nested in virgin material guide sleeve and secondary absorption virgin material guide shell and secondary absorption cloth awl on the secondary absorption discharge nozzle; Described secondary effluent unit comprises secondary absorption effluent weir and the secondary absorption rising pipe that is arranged on secondary cylindrical shell top;
Described discharging pipe connecting is connected to one-level sorbent material guide shell; Described one-level absorption effluent pipe coupling is to the secondary absorption water inlet pipe.
The utility model system adopts the two-stage tandem treatment process, and the water outlet of one-level adsorption unit can directly enter the secondary absorption device adsorbs, and also can entering all, other treatment process enter into the secondary absorption device after handling.
Simultaneously, new sorbent material adds in the secondary absorption device, and the sorbent material that secondary absorption is saturated can rise in the one-level adsorption unit, continues to use as sorbent material, and the saturated sorbent material of one-level absorption is promoted to outside the interior discharge system of waste tank.
Compared with prior art, the beneficial effects of the utility model are:
System's normal Inlet and outlet water when backwash; The water outlet of one-level adsorption unit can directly enter into the secondary absorption device and continue absorption, the water outlet of one-level adsorption unit can enter into other processing units, can enter the secondary absorption device after other unit water outlets, the use of can directly connecting also can increase other processing units therein; But system is works better when adding and draw off sorbent material; The one-level adsorption unit can utilize sorbent material saturated in the secondary absorption device, plays the effect of saving sorbent material; Simple to operate, easy to maintenance, sorbent material can be realized quantitatively adding and drawing off.
Description of drawings
Fig. 1 is system principle synoptic diagram of the present utility model;
Fig. 2 is the vertical view of the one-level backwash unit of the utility model one-level adsorption unit;
Fig. 3 is the vertical planning drawing of the one-level water inlet cloth water unit of the utility model one-level adsorption unit;
Fig. 4 is the vertical view of the one-level water inlet cloth water unit of the utility model one-level adsorption unit.
Among the figure: 1, one-level absorption water inlet pipe, 2, one-level absorption airlift pump inlet pipe, 3, one-level absorption discharge nozzle, 4, one-level absorption backwash inlet pipe, 5, one-level absorption backwash gas distribution pipe, 6, one-level absorption water distribution board, 7, one-level absorption water distribution awl, 8, one-level absorption airlift pump, 9, one-level absorption evacuated tube, 10, total evacuated tube, 11, the secondary absorption evacuated tube, 12, the secondary absorption airlift pump, 13, secondary absorption water distribution awl, 14, the secondary absorption water distribution board, 15, secondary absorption backwash gas distribution pipe, 16, the secondary absorption water inlet pipe, 17, secondary absorption airlift pump inlet pipe, 18, secondary absorption backwash inlet pipe, 19, the secondary absorption discharge nozzle, 20, secondary absorption cloth awl, 21, the secondary absorption rising pipe, 22, the secondary absorption airlift pump, 23, secondary absorption virgin material guide shell, 24, virgin material is carried reducing motor, 25, the virgin material conveying axis, 26, virgin material guide sleeve, 27, new hopper, 28, other processing unit rising pipe, 29, other processing unit, 30, the discharging pipe connecting, 31, one-level absorption effluent pipe, 32, one-level absorption effluent weir, 33, the backwash water discharge manifold, 34, one-level absorption drainage conduit, 35, one-level absorption backwash water shoot, 36, the secondary absorption bed, 37, the one-level adsorption bed, 38, one-level absorption cloth awl, 39, secondary absorption backwash water vent pipe, 40, one-level sorbent material guide shell, 41, secondary absorption backwash water discharge valve, 42, one-level absorption backwash water discharge valve.
Embodiment
As shown in the figure, the present embodiment technical scheme is as follows,
A kind of continuous adsorption system of sewage treatment process comprises the one-level adsorption unit and the secondary absorption device that connect with the series connection form;
Described one-level adsorption unit comprises one-level cylindrical shell, one-level water inlet cloth water unit, one-level air lift unit, one-level backwash unit, one-level feed unit, one-level adsorption bed 37, one-level water unit, described one-level water inlet cloth water unit comprises one-level absorption water inlet pipe 1, the one-level absorption water inlet pipe 1 bottom one-level absorption water distribution awl 7 of ining succession mutually arranges one-level absorption water distribution board 6 on the one-level absorption water distribution awl 7; Described one-level air lift unit comprises that the one-level that is arranged on one-level cylindrical shell bottom is adsorbed airlift pump 8 and coupled one-level is adsorbed airlift pump inlet pipe 2, one-level absorption airlift pump inlet pipe 2 picks out outside the one-level cylindrical shell, and 8 outlets of one-level absorption airlift pump connect one-levels absorption discharge nozzles 3 saturated sorbent material is put forward one-level absorption drainage conduit 34 to device top from one-level cylindrical shell bottom; Described one-level backwash unit comprises one-level absorption backwash inlet pipe 4, one-level absorption backwash gas distribution pipe 5, one-level absorption backwash water shoot 35 and one-level absorption backwash water discharge valve 42; Described one-level feed unit comprises discharging pipe connecting 30, is nested in one-level sorbent material guide shell 40 and one-level absorption cloth awl 38 on the one-level absorption discharge nozzle 3; Described one-level water unit comprises one-level absorption effluent weir 32 and the one-level absorption effluent pipe 31 that is arranged on cylindrical shell top;
Described secondary absorption device comprises secondary cylindrical shell, secondary water inlet cloth water unit, secondary air lift unit, secondary backwash unit, secondary feed unit, secondary absorption bed 36, secondary effluent unit, described secondary water inlet cloth water unit comprises secondary absorption water inlet pipe 16, the secondary absorption water inlet pipe 16 bottoms secondary absorption water distribution awl 13 of ining succession mutually arranges secondary absorption water distribution board 14 on the secondary absorption water distribution awl 13; Described secondary air lift unit comprises the secondary absorption airlift pump 12 that is arranged on secondary cylindrical shell bottom and coupled secondary absorption airlift pump inlet pipe 17, secondary absorption airlift pump inlet pipe 17 picks out outside the secondary cylindrical shell, and 12 outlets of secondary absorption airlift pump connect secondary absorption discharge nozzle 19 saturated sorbent material is carried to the discharging pipe connecting 30 on device top from secondary cylindrical shell bottom; Described secondary backwash unit comprises secondary absorption backwash inlet pipe 18, secondary absorption backwash gas distribution pipe 15, secondary absorption backwash water vent pipe 39 and secondary absorption backwash water discharge valve 42; Described secondary feed unit comprises new hopper 27, virgin material conveying reducing motor 24, virgin material conveying axis 25, is nested in virgin material guide sleeve 26 and secondary absorption virgin material guide shell 23 and secondary absorption cloth awl 20 on the secondary absorption discharge nozzle 19; Described secondary effluent unit comprises secondary absorption effluent weir 22 and the secondary absorption rising pipe 21 that is arranged on secondary cylindrical shell top;
Described discharging pipe connecting 30 is connected to one-level sorbent material guide shell 40; Described one-level absorption effluent pipe 31 is connected to secondary absorption water inlet pipe 16.
Between described one-level absorption effluent pipe 31 and the secondary absorption water inlet pipe 16 other processing unit 29 is set, other processing unit 29 is connecting secondary absorption water inlet pipe 16 by other processing unit rising pipe 28.Other processing unit 29 here refers to as biochemical system processing unit, chemical oxidation unit etc.
One-level absorption evacuated tube 9 and secondary absorption evacuated tube 11 are set respectively bottom one-level cylindrical shell and the secondary cylindrical shell and are pooled to total evacuated tube 10.
Secondary absorption backwash water water shoot 39, secondary absorption backwash water discharge valve 41 all are connected to backwash water discharge manifold 33 with one-level absorption backwash water shoot 35, one-level absorption backwash water discharge valve 42.
Have water outlet on the one-level absorption water distribution awl 7 in the described one-level water inlet cloth water unit, water outlet is followed one-level absorption water distribution board 6, one-level absorption water distribution board 6 inner hollow, and the bottom has sewage outlet; 7 to enter into one-level absorption water distribution board 6 inner and discharge from one-level absorption water distribution board 6 lower openings in the one-level absorption water distribution awl for sewage, one-level absorption water distribution board 6 internal space flowing water, top and other three sides all do not have water outlet, sewage is discharged from one-level absorption water distribution board lower openings and is made water distribution more even like this, be conducive to absorption, and one-level water inlet cloth water unit is difficult for blocking.Have water outlet on the secondary absorption water distribution awl 13 in the described secondary water inlet cloth water unit, water outlet is followed secondary absorption water distribution board 14, secondary absorption water distribution board 14 inner hollow, and the bottom has sewage outlet.
In the described one-level backwash unit, one-level absorption backwash water shoot 35 is one-level sorbent material guide shell 40 then; One-level absorption backwash inlet pipe 4 connects one-level absorption backwash gas distribution pipe 5 by one-level absorption cloth compression ring, and gas distribution is even.When being the one-level adsorption bed backwash of one-level adsorption unit, sorbent material in the discharging pipe connecting 30 stops feed, pressurized air enters into one-level absorption backwash gas distribution pipe 5 through one-level absorption backwash inlet pipe 4, qi-emitting hole from one-level absorption backwash gas distribution pipe spreads to one-level adsorption bed bottom, pressurized air will stick to the suspended substance on sorbent material top layer etc. and wash off from sorbent material, the suspended substance that backwash goes out enters into one-level sorbent material guide tube along with backwash water from bottom to top, enters one-level absorption backwash water pipe 35 then and discharges.In the described secondary backwash unit, secondary absorption backwash vent pipe 39 is secondary absorption virgin material guide shell 23 then; Secondary absorption backwash inlet pipe 18 connects secondary absorption backwash gas distribution pipe 15 by secondary absorption cloth compression ring.
Be nested with one-level sorbent material guide shell 40, one-level absorption cloth awl 38, one-level absorption cloth compression ring, one-level absorption water distribution awl 7 on the described one-level absorption discharge nozzle 3 from top to bottom successively; Be nested with virgin material guide sleeve 26, secondary absorption virgin material guide shell 23, secondary absorption cloth awl 20, secondary absorption cloth compression ring, secondary absorption water distribution awl 13 on the described secondary absorption discharge nozzle 19 from top to bottom successively;
Be arranged on one-level absorption effluent weir 32 upper edge height on the one-level cylindrical shell greater than one-level sorbent material guide shell 40 lower surface height; Be arranged on secondary absorption effluent weir 22 upper edge height on the secondary cylindrical shell greater than secondary absorption virgin material guide shell 23 lower surface height.
Described one-level absorption airlift pump inlet pipe 2 is being connected pneumatic plant respectively with secondary absorption airlift pump inlet pipe 17.
The utility model system is in sewage treatment process, and the water outlet of one-level adsorption unit can directly enter the secondary absorption device adsorbs, and also can entering all, other treatment process enter into the secondary absorption device after handling.Simultaneously, new sorbent material adds in the secondary absorption device automatically, and the sorbent material that secondary absorption is saturated can rise in the one-level adsorption unit, continues to use as sorbent material, and the saturated sorbent material of one-level absorption is promoted to outside the interior discharge system of waste tank.
As shown in the figure, the working process in production technique of the utility model system is as follows, sewage at first enters into one-level absorption water inlet pipe 1, sewage flow into one-level absorption water distribution board 6 from one-level absorption water inlet pipe 1 through one-level absorption water distribution awl 7, sewage is evenly distributed in the one-level cylindrical shell from one-level absorption water distribution board 6, sewage after absorption is upwards flowed through one-level adsorption bed 37 to one-level absorption effluent weir 32, absorption back water outlet is drained into other processing units 29 through one-level absorption effluent pipe 31, if do not establish other processing units 29, the one-level absorption effluent enters into secondary absorption water inlet pipe 16, if other processing units 29 are set, other processing unit rising pipe 28 water outlets flow into secondary absorption water distribution board 14 from secondary absorption water inlet pipe 16 through secondary absorption water distribution awl 13, sewage is evenly distributed in the secondary cylindrical shell from secondary absorption water distribution board 14, sewage after absorption is upwards flowed through secondary absorption bed 36 to secondary absorption effluent weir 22, and water outlet is flowed out through secondary absorption rising pipe 21 after the secondary absorption.
The sorbent material of storing in the new hopper 27 is periodically carried reducing motor 24 by virgin material, virgin material conveying axis 25 is sent in the virgin material fair water sleeves 26, and virgin material is evenly distributed in the secondary absorption bed through secondary absorption cloth awl 20 through secondary absorption virgin material guide shell 23 by fair water sleeves.Adsorb saturated sorbent material and pass through secondary absorption airlift pump 12 through secondary absorption discharge nozzle 19, discharging pipe connecting 30 enters into one-level sorbent material guide shell 40, and sorbent material is evenly distributed in the one-level adsorption bed through one-level absorption cloth awl 38.Sorbent material saturated in the one-level adsorption bed adsorbs airlift pump 8 outside one-level absorption discharge nozzle 3 is delivered to one-level absorption drainage conduit 34 discharge one-level cylindrical shells by one-level.
The power that one-level absorption airlift pump inlet pipe 2 provides pressurized air to promote as sorbent material for one-level absorption airlift pump 8.One-level absorption backwash inlet pipe 4 is connected to the backwash of one-level adsorption bed with one-level absorption backwash gas distribution pipe 5 pressurized air is provided.The power that secondary absorption airlift pump inlet pipe 17 provides pressurized air to promote as sorbent material for secondary absorption airlift pump 12.Secondary absorption backwash inlet pipe 18 provides pressurized air with secondary absorption backwash gas distribution pipe 15 for the backwash of secondary absorption bed.The backwash water that one-level adsorption bed backwash process produces drains into backwash main drain 33 through one-level absorption backwash water shoot 35, one-level absorption backwash water discharge valve 42, the backwash water that secondary absorption bed backwash process produces drains into backwash water discharge manifold 33 through secondary absorption backwash water shoot 39, secondary absorption backwash water discharge valve 41, and backwash water discharge manifold 33 drains into the prime treatment unit.One-level absorption evacuated tube 9 links to each other with total evacuated tube 10 with secondary absorption evacuated tube 11.
The utility model is not limited to above-described embodiment, and protection domain of the present utility model is all classified in any equivalent concepts or change in the technical scope that the utility model discloses as.
Claims (9)
1. the continuous adsorption system of a sewage treatment process is characterized in that: comprise the one-level adsorption unit and the secondary absorption device that connect with the series connection form;
Described one-level adsorption unit comprises one-level cylindrical shell, one-level water inlet cloth water unit, one-level air lift unit, one-level backwash unit, one-level feed unit, one-level adsorption bed (37), one-level water unit, described one-level water inlet cloth water unit comprises one-level absorption water inlet pipe (1), one-level absorption water inlet pipe (1) the bottom one-level absorption water distribution awl (7) of ining succession mutually arranges one-level absorption water distribution board (6) on the one-level absorption water distribution awl (7); Described one-level air lift unit comprises that the one-level that is arranged on one-level cylindrical shell bottom is adsorbed airlift pump (8) and coupled one-level is adsorbed airlift pump inlet pipe (2), one-level absorption airlift pump inlet pipe (2) picks out outside the one-level cylindrical shell, and one-level absorption airlift pump (8) outlet connects one-level absorption discharge nozzle (3) saturated sorbent material is put forward one-level absorption drainage conduit (34) to device top from one-level cylindrical shell bottom; Described one-level backwash unit comprises one-level absorption backwash inlet pipe (4), one-level absorption backwash gas distribution pipe (5), one-level absorption backwash water shoot (35) and one-level absorption backwash water discharge valve (42); Described one-level feed unit comprises discharging pipe connecting (30), is nested in one-level sorbent material guide shell (40) and one-level absorption cloth awl (38) on the one-level absorption discharge nozzle (3); Described one-level water unit comprises one-level absorption effluent weir (32) and the one-level absorption effluent pipe (31) that is arranged on cylindrical shell top;
Described secondary absorption device comprises secondary cylindrical shell, secondary water inlet cloth water unit, secondary air lift unit, secondary backwash unit, secondary feed unit, secondary absorption bed (36), secondary effluent unit, described secondary water inlet cloth water unit comprises secondary absorption water inlet pipe (16), secondary absorption water inlet pipe (16) the bottom secondary absorption water distribution awl (13) of ining succession mutually arranges secondary absorption water distribution board (14) on the secondary absorption water distribution awl (13); Described secondary air lift unit comprises the secondary absorption airlift pump (12) that is arranged on secondary cylindrical shell bottom and coupled secondary absorption airlift pump inlet pipe (17), secondary absorption airlift pump inlet pipe (17) picks out outside the secondary cylindrical shell, and secondary absorption airlift pump (12) outlet connects secondary absorption discharge nozzle (19) saturated sorbent material is carried to the discharging pipe connecting (30) on device top from secondary cylindrical shell bottom; Described secondary backwash unit comprises secondary absorption backwash inlet pipe (18), secondary absorption backwash gas distribution pipe (15), secondary absorption backwash water vent pipe (39) and secondary absorption backwash water discharge valve (41); Described secondary feed unit comprises new hopper (27), virgin material conveying reducing motor (24), virgin material conveying axis (25), is nested in virgin material guide sleeve (26) and secondary absorption virgin material guide shell (23) and secondary absorption cloth awl (20) on the secondary absorption discharge nozzle (19); Described secondary effluent unit comprises secondary absorption effluent weir (22) and the secondary absorption rising pipe (21) that is arranged on secondary cylindrical shell top;
Described discharging pipe connecting (30) is connected to one-level sorbent material guide shell (40); Described one-level absorption effluent pipe (31) is connected to secondary absorption water inlet pipe (16).
2. the continuous adsorption system of a kind of sewage treatment process as claimed in claim 1, it is characterized in that: between described one-level absorption effluent pipe (31) and the secondary absorption water inlet pipe (16) other processing unit (29) is set, other processing unit (29) is connecting secondary absorption water inlet pipe (16) by other processing unit rising pipe (28).
3. the continuous adsorption system of a kind of sewage treatment process as claimed in claim 1 or 2 is characterized in that: one-level absorption evacuated tube (9) and secondary absorption evacuated tube (11) are set respectively bottom one-level cylindrical shell and the secondary cylindrical shell and are pooled to total evacuated tube (10).
4. the continuous adsorption system of a kind of sewage treatment process as claimed in claim 1 or 2 is characterized in that: secondary absorption backwash water water shoot (39) all is connected to backwash water discharge manifold (33) with one-level absorption backwash water shoot (35).
5. the continuous adsorption system of a kind of sewage treatment process according to claim 1, it is characterized in that: have water outlet on the one-level absorption water distribution awl (7) in the described one-level water inlet cloth water unit, water outlet is followed one-level absorption water distribution board (6), one-level absorption water distribution board (6) inner hollow, and the bottom has sewage outlet; Have water outlet on the secondary absorption water distribution awl (13) in the described secondary water inlet cloth water unit, water outlet is followed secondary absorption water distribution board (14), secondary absorption water distribution board (14) inner hollow, and the bottom has sewage outlet.
6. the continuous adsorption system of a kind of sewage treatment process according to claim 1 is characterized in that: in the described one-level backwash unit, one-level absorption backwash water shoot (35) is one-level sorbent material guide shell (40) then; One-level absorption backwash inlet pipe (4) connects one-level absorption backwash gas distribution pipe (5) by one-level absorption cloth compression ring; In the described secondary backwash unit, secondary absorption backwash vent pipe (39) is secondary absorption virgin material guide shell (23) then; Secondary absorption backwash inlet pipe (18) connects secondary absorption backwash gas distribution pipe (15) by secondary absorption cloth compression ring.
7. the continuous adsorption system of a kind of sewage treatment process according to claim 1 is characterized in that: be nested with one-level sorbent material guide shell (40), one-level absorption cloth awl (38), one-level absorption cloth compression ring, one-level absorption water distribution awl (7) on the described one-level absorption discharge nozzle (3) from top to bottom successively; Be nested with virgin material guide sleeve (26), secondary absorption virgin material guide shell (23), secondary absorption cloth awl (20), secondary absorption cloth compression ring, secondary absorption water distribution awl (13) on the described secondary absorption discharge nozzle (19) from top to bottom successively.
8. the continuous adsorption system of a kind of sewage treatment process according to claim 1 is characterized in that: be arranged on upper edge, one-level absorption effluent weir (32) height on the one-level cylindrical shell greater than one-level sorbent material guide shell (40) lower surface height; Be arranged on secondary absorption effluent weir (22) upper edge height on the secondary cylindrical shell greater than secondary absorption virgin material guide shell (23) lower surface height.
9. the continuous adsorption system of a kind of sewage treatment process according to claim 1 is characterized in that: described one-level absorption airlift pump inlet pipe (2) is being connected pneumatic plant respectively with secondary absorption airlift pump inlet pipe (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320061065 CN203112546U (en) | 2013-02-03 | 2013-02-03 | Continuous adsorption system of sewage treatment process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320061065 CN203112546U (en) | 2013-02-03 | 2013-02-03 | Continuous adsorption system of sewage treatment process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203112546U true CN203112546U (en) | 2013-08-07 |
Family
ID=48892915
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320061065 Withdrawn - After Issue CN203112546U (en) | 2013-02-03 | 2013-02-03 | Continuous adsorption system of sewage treatment process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203112546U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103073088A (en) * | 2013-02-03 | 2013-05-01 | 大连涌清水处理技术有限公司 | Continuous adsorption system for sewage treatment process |
-
2013
- 2013-02-03 CN CN 201320061065 patent/CN203112546U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103073088A (en) * | 2013-02-03 | 2013-05-01 | 大连涌清水处理技术有限公司 | Continuous adsorption system for sewage treatment process |
| CN103073088B (en) * | 2013-02-03 | 2014-06-11 | 大连涌清水处理技术有限公司 | Continuous adsorption system for sewage treatment process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104084389A (en) | Ore washer | |
| CN203017830U (en) | Continuous type sand filter | |
| CN212757801U (en) | Gas circulation treatment glass steel washing tower | |
| CN103073088B (en) | Continuous adsorption system for sewage treatment process | |
| CN201578891U (en) | Novel sand filter | |
| CN203112546U (en) | Continuous adsorption system of sewage treatment process | |
| CN210711209U (en) | Device for supplementing carbon source by utilizing sludge hydrolysis fermentation | |
| CN104496126A (en) | Novel sewage treatment equipment | |
| CN205085051U (en) | Water conservation agricultural product cleaning machine | |
| CN204429042U (en) | A kind of active carbon inhales circulated sprinkling air peculiar smell scavenge unit | |
| CN204369728U (en) | A kind of New foul water disposal facility | |
| CN106006818A (en) | Multi-stage adsorption tower adopting phosphorus-removing granular active coke | |
| CN203144135U (en) | Continuous adsorption device in sewage treatment process | |
| CN203144136U (en) | Continuous adsorption device in sewage treatment process | |
| CN206447594U (en) | A kind of efficient ammonia nitrogen stripping tower | |
| CN204737825U (en) | Tailings overflow processing apparatus | |
| CN205323531U (en) | Container formula low concentration organic waste gas purification unit | |
| CN105967262A (en) | Dephosphorizing granular activated coke adsorption tower with fluidized bed | |
| CN103073118B (en) | Parallel-connected continuous adsorption system in wastewater treatment process | |
| CN204502527U (en) | Sewage-treatment plant | |
| CN203699975U (en) | Circulating-type oil-water separation device | |
| CN103539117A (en) | Continuous activated carbon washing and drying device | |
| CN204543925U (en) | A kind of multiple stage circulation washing absorption tower unit equipment | |
| CN101301539A (en) | Six-valve adsorption filter process and equipment | |
| CN203417505U (en) | High-efficiency quicksand filtration device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130807 Effective date of abandoning: 20140611 |
|
| RGAV | Abandon patent right to avoid regrant |