CN206232533U - A kind of containing wastewater from catalyst processing unit - Google Patents
A kind of containing wastewater from catalyst processing unit Download PDFInfo
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- CN206232533U CN206232533U CN201621290523.5U CN201621290523U CN206232533U CN 206232533 U CN206232533 U CN 206232533U CN 201621290523 U CN201621290523 U CN 201621290523U CN 206232533 U CN206232533 U CN 206232533U
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- vertical slot
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- outlet pipe
- web plate
- containing wastewater
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Abstract
The utility model discloses a kind of containing wastewater from catalyst processing unit, including filter chamber, flocculating chamber and ammonia aeration room, filter chamber side is provided with the first water inlet pipe, and opposite side is provided with the first outlet pipe, and sieve plate, activated carbon web plate and zeolite web plate are longitudinally plugged with filter chamber；The top of flocculating chamber is provided with the first cover plate, and the first cover plate is provided with flocculant dispensing kit, motor and soda acid dispensing kit, and the upper end of flocculating chamber is provided with the second outlet pipe；Three phase separator is provided with ammonia aeration room, shower is provided with below three phase separator, one end of shower is connected with the second outlet pipe, ammonia aeration room base plate is provided with aeration tube, one end of aeration tube is connected with air pump, the upper end of ammonia aeration room is provided with the 3rd outlet pipe.Containing wastewater from catalyst processing unit simple structure of the present utility model, it is easy to operate, can effectively remove suspension in containing wastewater from catalyst, heavy metal ion and ammonia nitrogen.
Description
Technical field
The utility model belongs to industrial waste water disposal device technical field, and in particular to a kind of containing wastewater from catalyst treatment dress
Put.
Background technology
At present, China's chemical industry has welcome good opportunity to develop, with the progress of chemical industry technology, catalyst
Species is on the increase, complicated component, and difficulty is brought to environmental improvement.On the other hand, China's economic market standardization, to environmental protection
Attention subsist benefit lifting, more require that our right combinations administer waste water, the harm that reduction is caused to environment.And containing wastewater from catalyst
Complicated component, typically contains the heavy metal ion of high concentration, and the fluctuation of ammonia nitrogen, suspension content is big, should not be entered using bioanalysis
Row treatment.Traditional containing wastewater from catalyst processing method is mainly makes heavy metal ion sink by adding flocculant in a heavy pond
Form sediment, the yield of this processing method sludge is big, and operating cost is high, and technique is unstable, and secondary clarifier effluent suspension is higher, goes out
Water water quality be difficult to it is up to standard, therefore, urgent need develops a kind of device of suitable containing wastewater from catalyst treatment.
Utility model content
The purpose of this utility model is to provide a kind of containing wastewater from catalyst processing unit, solves catalyst in the prior art and gives up
Water treatment facilities are more, complex process, operating cost is high, technique is unstable and effluent quality is difficult to problem up to standard.
The utility model provides a kind of containing wastewater from catalyst processing unit, including filter chamber, flocculating chamber and ammonia aeration room,
The upper end of the filter chamber side is provided with the first water inlet pipe, and the lower end of relative opposite side is provided with the first outlet pipe, described
In filter chamber from the first water inlet pipe side to the first outlet pipe side successively longitudinal direction and be arranged at intervals with dismountable sieve plate, can
The activated carbon web plate of dismounting and dismountable zeolite web plate, and the sieve plate is relative with first water inlet pipe, the filter
Web plate, the activated carbon web plate and the zeolite web plate are by rectangular frame and are arranged at double on the rectangular frame
Layer wire netting composition, one of the rectangular frame is detachably connected while adjacent with two, the activated carbon web plate pair
Activated carbon is filled between layer wire netting, zeolite is filled between the double-level-metal net of the zeolite web plate；
The lower end of the flocculating chamber is connected by the first outlet pipe with the filter chamber, and the top of the flocculating chamber is provided with
First cover plate, is disposed with flocculant dispensing kit, motor and soda acid dispensing kit, and offer on first cover plate
Dispensing mouth, offers poke hole in the middle of first cover plate, puddler, one end of the puddler are equipped with the poke hole
It is connected with the motor, pH value analyzer is additionally provided with the inwall of the flocculating chamber, the top of the flocculating chamber is set
There is the second outlet pipe；
The top of the ammonia aeration room is connected by the second outlet pipe with the flocculating chamber, and the top of the ammonia aeration room sets
The second cover plate is equipped with, the centre of second cover plate offers venthole, and second cover plate is arranged with three phase separator, institute
The escaping pipe for stating three phase separator is passed by the venthole, and shower, the shower are provided with the ammonia aeration room
It is connected with second outlet pipe positioned at the lower section of the three phase separator, and one end of the shower, the ammonia aeration
Aeration tube is provided with the base plate of room, the inlet end of the aeration tube is connected with the air pump outside the flocculating chamber, described
The lower end of ammonia aeration room is provided with the 3rd outlet pipe.
Preferably, longitudinal direction and the first vertical slot, the second vertical slot and the 3rd are arranged at intervals with side plate in the filter chamber
Vertical slot, is respectively arranged with the 4th vertical slot, the 5th vertical slot and the 6th vertical slot on relative another side plate, and first vertical slot with
4th vertical slot is relative, and second vertical slot is relative with the 5th vertical slot, the 3rd vertical slot and the 6th vertical slot phase
Right, detachable interposing is connected to sieve plate between first vertical slot and the 4th vertical slot, and second vertical slot is perpendicular with the described 5th
The active charcoal web plate of removable plug between groove, detachable interposing is connected to zeolite net between the 3rd vertical slot and the 6th vertical slot
Plate.
Preferably, the mesh of the double-level-metal net on the sieve plate, the activated carbon web plate and the zeolite web plate
Aperture is respectively less than 1mm.
Preferably, the activated carbon filled between the double-level-metal net of the activated carbon web plate is granular active carbon.
Preferably, the zeolite filled between the zeolite web plate double-level-metal net is particulate zeolite.
Preferably, a side side tenon adjacent with two of the rectangular frame connects.
Preferably, the brand of the three phase separator is Seiko, model FLQ1000A.
Preferably, first water inlet pipe, first outlet pipe, second outlet pipe and the 3rd outlet pipe
On be provided with valve.
Preferably, the bottom of the filter chamber, the flocculating chamber and the ammonia aeration room is provided with discharge pipeline.
Compared with prior art, the beneficial effects of the utility model are：
1) containing wastewater from catalyst processing unit of the present utility model is by setting filter chamber, and the longitudinally disposed filter in filter chamber
Web plate, activated carbon web plate and zeolite web plate, can remove most graininess suspension and colloid in containing wastewater from catalyst
Material, moreover it is possible to remove a part of ammonia nitrogen, and sieve plate, activated carbon web plate and zeolite web plate are that activity is plugged on filter chamber
In, can take out at any time, cleaning is convenient.
2) containing wastewater from catalyst processing unit of the present utility model is by setting flocculating chamber, and is flocculated toward addition in flocculating chamber
Agent, can take out most heavy metal ion in containing wastewater from catalyst, and soda acid dispensing kit and pH are additionally provided with flocculating chamber
Detector adjusts monitoring system pH value, can be smoothed out flocculation reaction, and can after flocculation reaction terminates, by waste water
Ammonia nitrogen regulation to generation ammonia state.
3) containing wastewater from catalyst processing unit of the present utility model is by setting ammonia aeration room come in stripping containing wastewater from catalyst
Ammonia nitrogen, and gas-liquid separation is carried out using three phase separator, simple structure is easy to operate.
Brief description of the drawings
Fig. 1 is the structural representation of the containing wastewater from catalyst processing unit that the utility model is provided；
Fig. 2 is the structural representation of the activated carbon web plate of the containing wastewater from catalyst processing unit that the utility model is provided.
Description of reference numerals：
1- filter chambers, 2- flocculating chambers, 3- ammonia aerations room, the water inlet pipes of 4- first, the outlet pipes of 5- first, 6- sieve plates, 7- lives
Property charcoal web plate, 8- zeolite web plates, 9- rectangular frames, 10- double-level-metal nets, the cover plates of 11- first, 12- flocculant dispensing kits, 13-
Motor, 14- soda acid dispensing kits, 15- puddlers, the outlet pipes of 16- second, the cover plates of 17- second, 18- three phase separators, 19-
Shower, 20- aeration tubes, 21- air pumps, the outlet pipes of 22- the 3rd.
Specific embodiment
Below in conjunction with the accompanying drawings, specific embodiment of the present utility model is described in detail, it is to be understood that this practicality
New protection domain is not limited by specific embodiment.
A kind of containing wastewater from catalyst processing unit, specifically as shown in Figure 1-2, including filter chamber 1, flocculating chamber 2 and ammonia aeration
Room 3, the upper end of the side of the filter chamber 1 is provided with the first water inlet pipe 4, and the lower end of relative opposite side is provided with the first outlet pipe
5, from the side of the first water inlet pipe 4 is to the side of the first outlet pipe 5 successively longitudinal direction and is arranged at intervals with dismountable in the filter chamber 1
Sieve plate 6, dismountable activated carbon web plate 7 and dismountable zeolite web plate 8, and the sieve plate 6 and the described first water inlet
Pipe 4 is relative, and the sieve plate 6, the activated carbon web plate 7 and the zeolite web plate 8 are by rectangular frame 9 and are arranged at institute
The double-level-metal net 10 stated on rectangular frame 9 is constituted, and one of the rectangular frame 9 detachably connects while adjacent with two
Connect, activated carbon, the double-level-metal net 10 of the zeolite web plate 8 are filled between the double-level-metal net 10 of the activated carbon web plate 7
Between be filled with zeolite；
The lower end of the flocculating chamber 2 is connected by the first outlet pipe 5 with the filter chamber 1, and the top of the flocculating chamber 2 sets
The first cover plate 11 is equipped with, flocculant dispensing kit 12, motor 13 and soda acid is disposed with first cover plate 11 and is thrown
Medicine-chest 14, and dispensing mouth is offered, poke hole is offered in the middle of first cover plate 11, it is equipped with puddler on the poke hole
15, one end of the puddler 15 is connected with the motor 13, and pH value measure is additionally provided with the inwall of the flocculating chamber 2
Instrument, the top of the flocculating chamber 2 is provided with the second outlet pipe 16；
The top of the ammonia aeration room 3 is connected by the second outlet pipe 16 with the flocculating chamber 2, the ammonia aeration room 3
Top is provided with the second cover plate 17, and the centre of second cover plate 17 offers venthole, and second cover plate 17 is arranged with
Three phase separator 18, the escaping pipe of the three phase separator 18 is passed by the venthole, is provided with the ammonia aeration room 3
Shower 19, the shower 19 be located at the three phase separator 18 lower section, and one end of the shower 19 with it is described
Second outlet pipe 16 is connected, and aeration tube 20, the inlet end of the aeration tube 20 and position are provided with the base plate of the ammonia aeration room 3
Air pump 21 outside the flocculating chamber 2 is connected, and the lower end of the ammonia aeration room 3 is provided with the 3rd outlet pipe 22.
Preferably, longitudinal direction and the first vertical slot, the second vertical slot and the 3rd are arranged at intervals with side plate in the filter chamber 1
Vertical slot, is respectively arranged with the 4th vertical slot, the 5th vertical slot and the 6th vertical slot on relative another side plate, and first vertical slot with
4th vertical slot is relative, and second vertical slot is relative with the 5th vertical slot, the 3rd vertical slot and the 6th vertical slot phase
Right, detachable interposing is connected to sieve plate 6 between first vertical slot and the 4th vertical slot, and second vertical slot is perpendicular with the described 5th
The active charcoal web plate 7 of removable plug between groove, detachable interposing is connected to zeolite between the 3rd vertical slot and the 6th vertical slot
Web plate 8.
Preferably, the double-level-metal net 10 on the sieve plate 6, the activated carbon web plate 7 and the zeolite web plate 8
Mesh aperture be respectively less than 1mm.
Preferably, the activated carbon filled between the double-level-metal net 10 of the activated carbon web plate 7 is granular active carbon.
Preferably, the zeolite filled between the double-level-metal net 10 of the zeolite web plate 8 is particulate zeolite.
In the utility model, longitudinally disposed first vertical slot and the 4th vertical slot in filter chamber 1, and the first vertical slot and the 4th perpendicular
Activity is plugged with sieve plate 6 between groove, and sieve plate 6 is by rectangular frame 9 and the double-level-metal net 10 being arranged on rectangular frame 9
Composition, the mesh aperture of double-level-metal net 10 is respectively less than 1mm, and double-level-metal net 10 can be to flowing into the catalyst in filter chamber 1
Big particulate matter and suspension are retained in waste water, so that most suspension in removing containing wastewater from catalyst.In order to reduce
The difficulty of subsequent treatment, activity is plugged with activated carbon between the second vertical slot and the 5th vertical slot of the utility model in filter chamber 1
Web plate 7, activated carbon web plate 7 is identical with the structure of sieve plate 6, and granular active carbon is filled between double-level-metal net 10,
Granular active carbon can further be purified to the water outlet of sieve plate 6, heavy metal ion and particle diameter in adsorption catalyst waste water
Less colloidal substance.The utility model is additionally provided with zeolite web plate 8 behind activated carbon web plate 7, is filled in zeolite web plate 8
There is zeolite, zeolite can carry out a certain degree of absorption, reduce ammonia-nitrogen content in waste water, subtract to the ammonia nitrogen in containing wastewater from catalyst
The light pressure of subsequent treatment ammonia nitrogen.
It should be noted that sieve plate 6, activated carbon web plate 7 and zeolite web plate 8 are all removably to be plugged on filter chamber
In vertical slot on 1 side plate, in sieve plate 6, activated carbon web plate 7 and the more influence of the surface deposits of zeolite web plate 8, it is acted on
Effect or in activated carbon web plate 7 and zeolite 8 adsorption saturation of web plate, can very easily by sieve plate 6, activated carbon web plate
7 and zeolite web plate 8 extracted out from vertical slot and cleared up, be inserted into being continuing with vertical slot after cleaning out.
Preferably, of the rectangular frame 9 is in the while movable joggle adjacent with other two.
In the utility model, the adjacent dismountable joggle of a side and other two of rectangular frame 9, for activated carbon
For web plate 7, when the charcoal absorption saturation filled in web plate, after being released from filter chamber 1, can be by rectangular frame 9
Active edges are opened, and then pour out the granular active carbon filled between double-level-metal net 10, are finally filled into new particle and are lived
Property charcoal can be adsorbed, be also such for the operation of zeolite web plate 8.
The utility model is provided with flocculating chamber 2, be provided with the first cover plate 11 of flocculating chamber 2 flocculant dispensing kit 12 and
Motor 13, flocculant dispensing kit 12 can be by mouth of offeing medicine at any time toward adding flocculant in flocculating chamber 2, and in puddler 15
Stirring under reacted with the heavy metal ion in waste water, heavy metal ion generation sediment is deposited in the bottom of flocculating chamber 2
Portion, so as to by the removal of heavy metal ions in waste water.Soda acid dispensing kit 14 is additionally provided with first cover plate 11 of flocculating chamber 2, acid
The one side of alkali dispensing kit 14 can add soda acid, and pH value of waste water is transferred into the requirement that suitable flocculation reaction occurs, and be flocculation reaction
It is smoothed out, on the other hand, toward adding alkali in flocculating chamber 2, pH value of waste water ammonia nitrogen in waste water is being transferred to after flocculation reaction terminates
With the state that ammonia form is present, then again leading to waste water carries out stripping in ammonia aeration room 3.
It should be noted that being additionally provided with pH value analyzer on the inwall of flocculating chamber 2, pH value analyzer being capable of real-time detection
The pH value of waste water in flocculating chamber 2, for addition soda acid amount provides foundation.
Preferably, the brand of the three phase separator 18 is Seiko, model FLQ1000A.
The utility model is provided with ammonia aeration room 3 to remove the ammonia nitrogen in containing wastewater from catalyst, and ammonia nitrogen passes through in flocculating chamber 2
Major part is converted into ammonia for the regulation of pH value, and the waste water containing ammonia enters ammonia aeration room 3 from the second outlet pipe 16, so
Waste water is sprayed downwards by the multiple spray apertures on shower 19, the air of the upward sprinkling of waste water and aeration tube 20 of sprinkling downwards
After contact, the ammonia blowout in waste water, the ammonia of blowout can be passed through the three phase separation of the model FLQ1000A of Seiko by air
The escaping pipe of device 18 enters gas collector, and the waste water after purification is flowed out by the 3rd outlet pipe 22, and by above-mentioned place
After reason, heavy metal ion and ammonia nitrogen in containing wastewater from catalyst are substantially achieved removal, discharged wastewater met the national standard.
Preferably, first water inlet pipe 4, first outlet pipe 5, second outlet pipe 16 and the described 3rd
Valve is provided with outlet pipe 22.
The utility model is equal on the first water inlet pipe 4, the first outlet pipe 5, the second outlet pipe 16 and the 3rd outlet pipe 22
It is provided with valve.Valve on first water inlet pipe 4 can control waste water to enter the time of filter chamber 1, the valve on the first outlet pipe 5
Door can control the waste water handled well in filter chamber 1 to enter the time of flocculating chamber 2, and have enough waste water to enter flocculating chamber
The valve closed after 2 on first outlet pipe 5, also simultaneously closes off the valve on the second outlet pipe 16, completes and sinks in flocculation reaction
The valve on the second outlet pipe 16 is opened after the certain hour of shallow lake, the clarified wastewater allowed in flocculating chamber 2 carries out ammonia into ammonia aeration room 3
Stripping, ammonia aeration finishes the valve opened on the 3rd outlet pipe 22, will process qualified waste water discharge.
Preferably, the bottom of the filter chamber 1, the flocculating chamber 2 and the ammonia aeration room 3 is provided with discharge pipeline.
It is heavy to discharge that the utility model is provided with discharge pipeline in the bottom of filter chamber 1, flocculating chamber 2 and ammonia aeration room 3
Product thing, cleaning is convenient, and only need to open spoil disposal tube valve can remove with by deposit, easy to operate.
In the utility model, disclosed above is only specific embodiment of the utility model, but, the utility model is implemented
Example is not limited to this, and the changes that any person skilled in the art can think of should all fall into protection domain of the present utility model.
Claims (9)
1. a kind of containing wastewater from catalyst processing unit, it is characterised in that including filter chamber (1), flocculating chamber (2) and ammonia aeration room
(3), the upper end of filter chamber (1) side is provided with the first water inlet pipe (4), and the lower end of relative opposite side is provided with first and goes out
Water pipe (5), the filter chamber (1) is interior longitudinal successively from the first water inlet pipe (4) side to the first outlet pipe (5) side and interval sets
It is equipped with dismountable sieve plate (6), dismountable activated carbon web plate (7) and dismountable zeolite web plate (8), and the filter screen
Plate (6) is relative with first water inlet pipe (4), the sieve plate (6), the activated carbon web plate (7) and the zeolite web plate
(8) constituted by rectangular frame (9) and the double-level-metal net (10) being arranged on the rectangular frame (9), the rectangle frame
One of frame (9) is detachably connected while adjacent with two, is filled out between the double-level-metal net (10) of the activated carbon web plate (7)
Filled with activated carbon, zeolite is filled between the double-level-metal net (10) of the zeolite web plate (8)；
The lower end of the flocculating chamber (2) is connected by the first outlet pipe (5) with the filter chamber (1), the top of the flocculating chamber (2)
End be provided with the first cover plate (11), be provided with first cover plate (11) flocculant dispensing kit (12), motor (13) with
And soda acid dispensing kit (14), and dispensing mouth is offered, poke hole is offered in the middle of first cover plate (11), on the poke hole
Be equipped with puddler (15), one end of the puddler (15) is connected with the motor (13), the flocculating chamber (2) it is interior
PH value analyzer is additionally provided with wall, the top of the flocculating chamber (2) is provided with the second outlet pipe (16)；
The top of the ammonia aeration room (3) is connected by second outlet pipe (16) with the flocculating chamber (2), the ammonia aeration
The top of room (3) is provided with the second cover plate (17), and the centre of second cover plate (17) offers venthole, second cover plate
(17) three phase separator (18) is arranged with, the escaping pipe of the three phase separator (18) is passed by the venthole, described
Shower (19) is provided with ammonia aeration room (3), the shower (19) positioned at the lower section of the three phase separator (18), and
One end of the shower (19) is connected with second outlet pipe (16), and exposure is provided with the base plate of the ammonia aeration room (3)
Tracheae (20), the inlet end of the aeration tube (20) is connected with positioned at the flocculating chamber (2) outside air pump (21), and the ammonia blows
The lower end of de- room (3) is provided with the 3rd outlet pipe (22).
2. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the interior side plate of the filter chamber (1)
Upper longitudinal direction and the first vertical slot, the second vertical slot and the 3rd vertical slot are arranged at intervals with, is respectively arranged with relative another side plate
Four vertical slots, the 5th vertical slot and the 6th vertical slot, and first vertical slot is relative with the 4th vertical slot, second vertical slot and institute
State the 5th vertical slot relative, the 3rd vertical slot is relative with the 6th vertical slot, between first vertical slot and the 4th vertical slot
Detachable interposing is connected to sieve plate (6), the active charcoal web plate of removable plug between second vertical slot and the 5th vertical slot
(7), detachable interposing is connected to zeolite net plate (8) between the 3rd vertical slot and the 6th vertical slot.
3. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the sieve plate (6), the activity
The mesh aperture of the double-level-metal net (10) on charcoal web plate (7) and the zeolite web plate (8) is respectively less than 1mm.
4. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the activated carbon web plate (7) it is double
The activated carbon filled between layer wire netting (10) is granular active carbon.
5. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the double-deck gold of the zeolite web plate (8)
The zeolite filled between category net (10) is particulate zeolite.
6. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that of the rectangular frame (9)
The side side tenon adjacent with two connects.
7. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the product of the three phase separator (18)
Board is Seiko, model FLQ1000A.
8. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that first water inlet pipe (4), described
Valve is provided with first outlet pipe (5), second outlet pipe (16) and the 3rd outlet pipe (22).
9. containing wastewater from catalyst processing unit according to claim 1, it is characterised in that the filter chamber (1), the flocculation
The bottom of room (2) and the ammonia aeration room (3) is provided with discharge pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621290523.5U CN206232533U (en) | 2016-11-29 | 2016-11-29 | A kind of containing wastewater from catalyst processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621290523.5U CN206232533U (en) | 2016-11-29 | 2016-11-29 | A kind of containing wastewater from catalyst processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206232533U true CN206232533U (en) | 2017-06-09 |
Family
ID=58979852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621290523.5U Expired - Fee Related CN206232533U (en) | 2016-11-29 | 2016-11-29 | A kind of containing wastewater from catalyst processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206232533U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751564A (en) * | 2018-06-13 | 2018-11-06 | 宁波新桥环境工程咨询有限公司 | A kind of Heavy Metal Pollution in Water Environment controlling device |
-
2016
- 2016-11-29 CN CN201621290523.5U patent/CN206232533U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751564A (en) * | 2018-06-13 | 2018-11-06 | 宁波新桥环境工程咨询有限公司 | A kind of Heavy Metal Pollution in Water Environment controlling device |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170609 Termination date: 20171129 |
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| CF01 | Termination of patent right due to non-payment of annual fee |