CN209530305U - A kind of chemistry station-service multimedium effluent filter - Google Patents
A kind of chemistry station-service multimedium effluent filter Download PDFInfo
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- CN209530305U CN209530305U CN201920192918.9U CN201920192918U CN209530305U CN 209530305 U CN209530305 U CN 209530305U CN 201920192918 U CN201920192918 U CN 201920192918U CN 209530305 U CN209530305 U CN 209530305U
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Abstract
The utility model provides a kind of chemical station-service multimedium effluent filter, belong to technical field of sewage, including tank body, drainpipe and water inlet pipe, it is respectively embedded into from top to bottom on the right side of tank body and is provided with water inlet pipe and drainpipe, and drainpipe is arranged in " L " shape, tank body top has been bolted to connection access hole, and water inlet pipe is fixedly connected with water segregator close to tank interior one end.Top cap, the first active carbon layer and the second charcoal canister are set in this kind chemistry station-service multimedium effluent filter, pass through being used cooperatively for top cap and water segregator, it is flowed so that sewage is shunted in water inlet pipe to water segregator, and then enable sewage in sprinkling shape discharge upwards, achieved the purpose that by increasing time of contact between sewage and air to sewage cooling, the first active carbon layer and the dual cooperation of the second charcoal canister are utilized simultaneously, so that the sewage that primary filtration finishes further filters in the two, so that the impurity in sewage be enabled to reach better filter effect by Activated carbon separation.
Description
Technical field
The utility model relates to technical field of sewage, more specifically, being related to a kind of multimedium effluent filter.
Background technique
Industrial wastewater includes production waste water, production waste and cooling water, refer to the waste water generated in industrial processes and
Waste liquid, wherein containing the pollution generated in industrial production materials, intermediate product, byproduct and the production process outflowed with water
Object, industrial wastewater is many kinds of, complicated component, such as contains mercury in electrolytic salt industrial wastewater, and heavy metal metallurgy industry waste water contains
The various metals such as lead, cadmium contain in petroleum refining industry waste water containing each heavy metal species such as cyanide and chromium in metal plating waste water
Phenol, containing various pesticides etc. in pesticide process industry waste water, due to, often containing there are many noxious materials, polluting environment pair in industrial wastewater
Human health has very big harm, therefore wants Development & Multipurpose use, turns harm into good, and according to Pollutants in Wastewater ingredient and concentration,
It can just be discharged after taking corresponding control techniques to be disposed.
Wherein when carrying out sewage treatment, people devise a kind of more medium filter, and more medium filter is to utilize one
The higher water of turbidity is passed through certain thickness granular or non-grain material under pressure by kind or several filter mediums, from
And effectively removing suspended impurity makes the process of clarification of water, common filtrate has quartz sand, anthracite, manganese sand etc., is mainly used for
Water process turbidity removal, softened water, prime pretreatment of pure water etc., delivery turbidity is up to 3 degree hereinafter, but existing more medium filter
When carrying out sewage treatment, since individual sewage temperatures are higher, if sewage is directly contacted with filter structure, to filter structure meeting
It causes compared with macrolesion, and then influences the service life of filter structure, while existing filter structure is mostly by the quartzy material of multilayer
Material is filtered separation, though simple structure, is unable to reach preferable using effect.
Therefore, it is necessary to further be studied on the basis of existing multimedium effluent filter, a kind of new change is provided
Learn station-service multimedium effluent filter.
Utility model content
The utility model is intended to solve existing multimedium effluent filter can not carry out cooling and sewage to sewage
The bad technical problem for the treatment of effect, provides a kind of chemical station-service multimedium effluent filter, which centers top cap, first
Active carbon layer and the second charcoal canister, by being used cooperatively for top cap and water segregator, so that sewage is shunted in water inlet pipe to dividing water
Device flowing, and then enable sewage in sprinkling shape discharge upwards, reach cold to sewage by increasing time of contact between sewage and air
But purpose, while the first active carbon layer and the dual cooperation of the second charcoal canister are utilized, so that the sewage that primary filtration finishes exists
It is further filtered in the two, so that the impurity in sewage be enabled to reach better filter effect by Activated carbon separation.
To achieve the above object, the utility model provides the following technical solutions: a kind of chemistry station-service multimedium sewage water filtration
Device, including tank body, drainpipe and water inlet pipe, the tank body right side is respectively embedded into from top to bottom is provided with water inlet pipe and drainpipe,
And drainpipe is arranged in " L " shape；
The tank body top has been bolted to connection access hole, and the water inlet pipe is close to the fixed company in tank interior one end
It is connected to water segregator, the water segregator top is nested top cap, and the tank interior is sequentially filled from top to bottom is provided with nothing
Bituminous coal layer, fine sand layer, coarse sands layer, sandy gravel stratum and the first active carbon layer, the tank interior bottom end were fixedly connected with filter bottom tower,
The filter bottom tower excessively, which is internally embedded, is provided with the second charcoal canister, and the filter bottom tower opening of external wall of crossing is provided with draining pore, institute
Stating tank interior link has the first separating plate, is fixedly connected with intercept net inside first separating plate.
Further preferred embodiment: between the anthracite coal measure, fine sand layer, coarse sands layer, sandy gravel stratum and the first active carbon layer
The big minispread of thickness is followed successively by anthracite coal measure > fine sand layer > coarse sands layer > sandy gravel stratum the first active carbon layer of >, and above structure it
Between be equipped with stainless steel strainer.
Further preferred embodiment: first active carbon layer lower end is in " rotary table " shape setting, and the first active carbon layer
Lower surface center is equipped with through-hole, while being in closed state between through-hole and the first active carbon layer edge.
Further preferred embodiment: the gap 1.5cm is equipped in the middle part of the top cap between fraction water device water-dividing device inner wall, and is pushed up
The setting in a circular table shape of crown end.
Further preferred embodiment: the mesh-density of the intercept net is 1cm.
Further preferred embodiment: the filter bottom top of tower of crossing is equipped with diameter opening greater than the first active carbon layer central through hole
Mouthful, and be open in " up big and down small " setting.
Further preferred embodiment: active carbon packed density is greater than in the first active carbon layer inside second charcoal canister
1.5 times of portion's active carbon packed density.
The utility model has the advantages that
1, the chemical station-service multimedium effluent filter of this kind, by the way that top cap is arranged, so that cooperating between top cap and water segregator
It uses, is flowed so that sewage is shunted in water inlet pipe to water segregator, and then enable sewage in sprinkling shape discharge upwards, by increasing sewage
Time of contact achievees the purpose that cooling to sewage between air.
2, to carry out quick separating to the large volume impurity in sewage, the first separating plate is set in tank interior, utilizes the
Intercept net in one separating plate carries out the large volume impurity in sewage quickly to intercept separation, and then accelerates the subsequent filtering of sewage
Step improves sewage treatment speed.
3, to obtain better filter effect, using the first active carbon layer and the dual cooperation of the second charcoal canister, so that
The sewage that primary filtration finishes further filters in the two, so that the impurity in sewage be enabled to reach better by Activated carbon separation
Filter effect.
Detailed description of the invention
Fig. 1 is the overall structure diagram of the utility model.
Fig. 2 is the whole the schematic diagram of the section structure of the utility model.
Fig. 3 is the first separating plate top plan view structural schematic diagram of the utility model.
Fig. 4 is Fig. 2 enlarged structure schematic diagram of the utility model.
Fig. 5 crosses filter bottom tower the schematic diagram of the section structure for the utility model.
In Fig. 1-5: 1- tank body；101- drainpipe；102- water inlet pipe；1021- water segregator；1022- top cap；103- maintenance
Mouthful；104- anthracite coal measure；105- fine sand layer；106- coarse sands layer；107- sandy gravel stratum；The first active carbon layer of 108-；109- crosses filter bottom
Tower；The second charcoal canister of 1091-；1092- drains pore；The first separating plate of 2-；201- intercept net.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Please refer to Fig. 1-5, in the utility model embodiment, a kind of chemistry station-service multimedium effluent filter, including tank body
1, drainpipe 101, water inlet pipe 102, water segregator 1021, top cap 1022, access hole 103, anthracite coal measure 104, fine sand layer 105, thick
Layer of sand 106, sandy gravel stratum 107, the first active carbon layer 108, cross filter bottom tower 109, the second charcoal canister 1091, draining pore 1092,
First separating plate 2 and intercept net 201,1 right side of tank body is respectively embedded into from top to bottom is provided with water inlet pipe 102 and drainpipe 101, and
Drainpipe 101 is arranged in " L " shape, and 1 top of tank body has been bolted to connection access hole 103, and water inlet pipe 102 is close to tank body 1
Internal one end is fixedly connected with water segregator 1021, and 1021 top of water segregator is nested top cap 1022, inside tank body 1 from upper and
Under be sequentially filled and be provided with anthracite coal measure 104, fine sand layer 105, coarse sands layer 106, sandy gravel stratum 107 and the first active carbon layer 108, tank
1 inner bottom of body was fixedly connected with filter bottom tower 109, and filter bottom tower 109, which is internally embedded, excessively is provided with the second charcoal canister 1091, mistake
109 opening of external wall of filter bottom tower is provided with draining pore 1092, and tank body 1, which is internally embedded, is connected with the first separating plate 2, the first separating plate
Intercept net 201 is fixedly connected with inside 2.
In the utility model embodiment, preferred embodiment, anthracite coal measure 104, fine sand layer 105, coarse sands layer 106, sandy gravel stratum 107
And first the big minispread of thickness between active carbon layer 108 be followed successively by 104 > fine sand layer of anthracite coal measure, 105 > coarse sands layer, 106 > sand
107 the first active carbon layer of > 108 of gravel bed, and stainless steel strainer is equipped between above structure, so that above structure reduction accounts for
With space, and then reduce 1 volume of tank body；First active carbon layer, 108 lower end is in " rotary table " shape setting, and the first active carbon layer
108 lower surfaces center are equipped with through-hole, while being in closed state between 108 edge of through-hole and the first active carbon layer, so that sewage collection
It is middle to be flowed into filter bottom tower 109 excessively, improved the filter efficiency of filter bottom tower 109；Water is divided with water segregator 1021 in 1022 middle part of top cap
Be equipped with the gap 1.5cm between device inner wall, and 1022 top of top cap setting in a circular table shape so that top cap 1022 and water segregator 1021 it
Between be used cooperatively so that sewage water inlet pipe 102 shunt to water segregator 1021 flow, and then enable sewage in upwards sprinkling shape row
Out, achieved the purpose that by increasing time of contact between sewage and air to sewage cooling；The mesh-density of intercept net 201 is
1cm can intercept the large volume impurity in the sewage flowed out in water segregator 1021, and then accelerate the subsequent filtration step of sewage, mention
High sewage treatment speed；It crosses at the top of filter bottom tower 109 and is equipped with the opening that diameter is greater than 108 central through hole of the first active carbon layer, and open
Mouth is greater than inside the first active carbon layer 108 in " up big and down small " setting, 1091 inside active carbon packed density of the second charcoal canister
1.5 times of active carbon packed density, using the first active carbon layer 108 and the dual cooperation of the second charcoal canister 1091, so that tentatively
It filters the sewage finished further to filter in the two, so that the impurity in sewage be enabled to reach better filtering by Activated carbon separation
Effect.
Working principle
In chemical station-service multimedium effluent filter a kind of using the utility model, firstly, needed for tank body 1 is mounted on
Operating position, then drainpipe 101 and water inlet pipe 102 are tightly connected with extraneous corresponding water pipe respectively, then can will
Untreated sewage is conveyed by water inlet pipe 102 into tank body 1, and when sewage reaches 1021 position of water segregator, sewage is in water
It is flowed under the driving of flowing pressure to water segregator 1021, and then sewage is enabled, in sprinkling shape discharge upwards, to pass through increasing by top cap 1022
Time of contact between sewage and air is added to achieve the purpose that, to sewage cooling, the sewage then sprayed is fallen under the effect of gravity
Under, while being contacted with intercept net 201, the large volume impurity in sewage is carried out using intercept net 201 quickly to intercept separation, then
Sewage passes through the multiple filtration of anthracite coal measure 104, fine sand layer 105, coarse sands layer 106, sandy gravel stratum 107 and the first active carbon layer 108
It flowed at 109 upper opening of filter bottom tower, then by crossing the second further filtering of charcoal canister 1091 inside filter bottom tower 109,
It is discharged finally by internal and external pressure difference by draining pore 1092, then is conveyed outward by drainpipe 101.
This kind chemistry station-service multimedium effluent filter has wide applicability, to solve to propose in above-mentioned background technique
Existing multimedium effluent filter cooling and bad wastewater treatment efficiency problem can not be carried out to sewage.
The above are merely preferred embodiments of the present invention, it is noted that for those skilled in the art,
Without departing from the concept of the premise utility, several modifications and improvements can also be made, these also should be considered as practical
Novel protection scope, these all will not influence the effect and patent practicability of the utility model implementation.
Claims (7)
1. a kind of chemistry station-service multimedium effluent filter, including tank body (1), drainpipe (101) and water inlet pipe (102), described
It is respectively embedded into from top to bottom on the right side of tank body (1) and is provided with water inlet pipe (102) and drainpipe (101), and drainpipe (101) is in " L "
Shape setting；
It is characterized by: tank body (1) top has been bolted to connection access hole (103), the water inlet pipe (102) is leaned on
Nearly internal one end of tank body (1) is fixedly connected with water segregator (1021), and water segregator (1021) top is nested top cap
(1022), it is sequentially filled from top to bottom inside the tank body (1) and is provided with anthracite coal measure (104), fine sand layer (105), coarse sands layer
(106), sandy gravel stratum (107) and the first active carbon layer (108), tank body (1) inner bottom were fixedly connected with filter bottom tower
(109), filter bottom tower (109) excessively, which are internally embedded, is provided with the second charcoal canister (1091), described to cross filter bottom tower (109) outer wall
Opening is provided with draining pore (1092), and the tank body (1), which is internally embedded, to be connected with the first separating plate (2), first separation
Intercept net (201) are fixedly connected with inside plate (2).
2. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: the anthracite coal measure
(104), the big minispread of thickness between fine sand layer (105), coarse sands layer (106), sandy gravel stratum (107) and the first active carbon layer (108)
It is followed successively by anthracite coal measure (104) > fine sand layer (105) > coarse sands layer (106) > sandy gravel stratum (107) first active carbon layer of >
(108), and between above structure it is equipped with stainless steel strainer.
3. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: first active carbon layer
(108) lower end is in falling the setting of " rotary table " shape, and the first active carbon layer (108) lower surface center is equipped with through-hole, while through-hole and the
It is in closed state between one active carbon layer (108) edge.
4. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: in the top cap (1022)
The gap 1.5cm, and the setting in a circular table shape of top cap (1022) top are equipped between portion and water segregator (1021) water segregator inner wall.
5. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: the intercept net (201)
Mesh-density be 1cm.
6. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: described to cross filter bottom tower
(109) top is equipped with the opening that diameter is greater than the first active carbon layer (108) central through hole, and is open in " up big and down small " setting.
7. chemistry station-service multimedium effluent filter according to claim 1, it is characterised in that: second charcoal canister
(1091) internal active carbon packed density is greater than 1.5 times of the first active carbon layer (108) internal active carbon packed density.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920192918.9U CN209530305U (en) | 2019-02-13 | 2019-02-13 | A kind of chemistry station-service multimedium effluent filter |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920192918.9U CN209530305U (en) | 2019-02-13 | 2019-02-13 | A kind of chemistry station-service multimedium effluent filter |
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| CN209530305U true CN209530305U (en) | 2019-10-25 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110711413A (en) * | 2019-11-13 | 2020-01-21 | 李洁洁 | Industrial water filter |
| CN112408664A (en) * | 2020-11-16 | 2021-02-26 | 广东石油化工学院 | Catalytic cracking catalyst production wastewater pretreatment system and method |
-
2019
- 2019-02-13 CN CN201920192918.9U patent/CN209530305U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110711413A (en) * | 2019-11-13 | 2020-01-21 | 李洁洁 | Industrial water filter |
| CN112408664A (en) * | 2020-11-16 | 2021-02-26 | 广东石油化工学院 | Catalytic cracking catalyst production wastewater pretreatment system and method |
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