CN206417935U - Advanced waste treatment system - Google Patents
Advanced waste treatment system Download PDFInfo
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- CN206417935U CN206417935U CN201621460296.6U CN201621460296U CN206417935U CN 206417935 U CN206417935 U CN 206417935U CN 201621460296 U CN201621460296 U CN 201621460296U CN 206417935 U CN206417935 U CN 206417935U
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Abstract
The utility model discloses a kind of advanced waste treatment system, the advanced waste treatment system includes：Fenton's reaction device, the Fenton's reaction device includes having the Fenton's reaction chamber being sequentially communicated along waste water treatment process direction, PH readjustments chamber, adsorbent chamber and Fenton flocculation chamber in Fenton's reaction pond, the Fenton's reaction pond；There is the Fenton's reaction chamber acid to add, and mouth, catalyst add mouth and oxidant adds mouth；There is the PH readjustments chamber alkali to add mouth；There is the adsorbent chamber adsorbent to add mouth；The Fenton flocculation chamber has flocculant concentration mouthful.COD high treating effects, simple in construction, low cost and other advantages are had according to the advanced waste treatment system of the utility model embodiment.
Description
Technical field
The utility model is related to environmental technology field, in particular to a kind of advanced waste treatment system.
Background technology
In waste water treatment process in correlation technique, its Fenton (FENTON) advanced treatment system using ferrous sulfate or its
Its chemical reagent is as catalyst, and hydrogen peroxide or other chemical reagent are as oxidant, by waste water under the conditions of certain pH
COD (organic pollution) be oxidized to carbon dioxide and water.When the difficult degradation COD concentration in waste water is higher, Fenton is only relied on
Technique is unable to reach requirement, therefore is generally led in the follow-up increase activated-charcoal column isoreactivity charcoal processing unit of Fenton's reaction device
Cause complicated, cost higher.
Utility model content
The utility model is intended at least solve one of above-mentioned technical problem in correlation technique to a certain extent.Therefore,
The utility model proposes a kind of advanced waste treatment system, the advanced waste treatment system has COD high treating effects, structure letter
Single, low cost and other advantages.
To achieve the above object, a kind of advanced waste treatment system is proposed according to embodiment of the present utility model, it is described useless
Water depth processing system includes：Fenton's reaction device, the Fenton's reaction device includes Fenton's reaction pond, the Fenton's reaction pond
It is interior to adjust back chamber, adsorbent chamber and Fenton flocculation chamber with the Fenton's reaction chamber being sequentially communicated along waste water treatment process direction, PH；It is described
There is Fenton's reaction chamber acid to add, and mouth, catalyst add mouth and oxidant adds mouth；There is the PH readjustments chamber alkali to add mouth；Institute
Stating adsorbent chamber, there is adsorbent to add mouth；The Fenton flocculation chamber has flocculant concentration mouthful.
COD high treating effects, simple in construction, cost are had according to the advanced waste treatment system of the utility model embodiment
Low advantage.
In addition, can also have technology additional as follows special according to the advanced waste treatment system of the utility model embodiment
Levy：
According to one embodiment of the present utility model, the Fenton's reaction pond is provided with what is connected with the Fenton's reaction chamber
First stirring air intake；And/or the Fenton's reaction intracavitary is provided with the first Fenton mixer.
According to one embodiment of the present utility model, the Fenton's reaction pond is provided with adjusts back chamber is connected the with the PH
Two stirring air intakes；And/or the PH readjustments intracavitary is provided with the second Fenton mixer.
According to one embodiment of the present utility model, the Fenton's reaction pond is provided with the 3rd connected with the adsorbent chamber
Stir air intake；And/or the 3rd Fenton mixer is provided with the adsorbent chamber.
According to one embodiment of the present utility model, the Fenton's reaction pond is provided with the 3rd connected with the adsorbent chamber
Air intake is stirred, the advanced waste treatment system also includes：Air delivery pipe is stirred, the stirring air delivery pipe is by institute
The 3rd stirring air intake is stated to stretch into the adsorbent chamber.
According to one embodiment of the present utility model, the Fenton flocculation intracavitary is provided with the 4th Fenton mixer；And/or institute
State Fenton's reaction pond and be provided with the 4th stirring air intake connected with Fenton flocculation chamber.
According to one embodiment of the present utility model, the advanced waste treatment system also includes：Acid adds pipe, the acid
Add pipe and add mouth with the acid and connect；Catalyst adds pipe, and the catalyst, which adds pipe and adds mouth with the catalyst, to be connected；
Oxidant adds pipe, and the oxidant, which adds pipe and adds mouth with the oxidant, to be connected；Alkali adds pipe, and the alkali adds pipe and institute
State alkali and add mouth connection；Adsorbent adds pipe, and the adsorbent, which adds pipe and adds mouth with the adsorbent, to be connected；Flocculant concentration
Pipe, the flocculant concentration pipe is connected with the flocculant concentration mouthful.
According to one embodiment of the present utility model, it is provided with the Fenton's reaction pond and separates the Fenton's reaction chamber and institute
State the first dividing plate of PH readjustment chambers, separate PH readjustment chamber and the second partition of the adsorbent chamber and separate the adsorbent chamber and
The bottom of the lower end and the Fenton's reaction pond of 3rd dividing plate of the Fenton flocculation chamber, first dividing plate and the 3rd dividing plate
Wall is connected, and the lower end of the second partition is spaced apart with the bottom wall in the Fenton's reaction pond and upper end is higher than first dividing plate
Upper end and the upper end of the 3rd dividing plate.
According to one embodiment of the present utility model, the Fenton's reaction device also includes Fenton sedimentation basin, the Fenton
Reaction tank is sequentially communicated with the Fenton sedimentation basin along the waste water treatment process direction.
According to one embodiment of the present utility model, the advanced waste treatment system also includes：Continuous sand filter, it is described
Continuous sand filter is connected with the Fenton sedimentation basin, and the continuous filter sand utensil has compressed air inlet and sand filtration flushing water to go out
Mouthful, the sand filtration is rinsed water out and connected with the Fenton's reaction chamber or the Fenton sedimentation basin in the Fenton's reaction pond.
Brief description of the drawings
Fig. 1 is the structural representation of the advanced waste treatment system according to the utility model embodiment.
Fig. 2 is the structural representation of the advanced waste treatment system according to the utility model another embodiment.
Reference：
Advanced waste treatment system 60,
Fenton's reaction device 4100,
Fenton's reaction pond 4110, Fenton's reaction chamber 4111, PH readjustment chamber 4115, adsorbent chamber 4116, Fenton flocculation chamber 4112,
Acid add mouth 4121, catalyst add mouth 4122, oxidant add mouth 4123, alkali add mouth 4124, adsorbent add mouth 4125,
Flocculant concentration mouthful the 4126, first Fenton mixer 4113, the second Fenton mixer 4117, the 3rd Fenton mixer 4118, the
Four Fenton mixers the 4114, the 3rd stirring air intake 4127, stirring air delivery pipe 4128, the first dividing plate 4141, second every
Plate 4142, the 3rd dividing plate 4143,
Fenton sedimentation basin 4130, Fenton mud scraper 4132,
Acid add pipe 4131, catalyst add pipe 4132, oxidant add pipe 4133, alkali add pipe 4134, adsorbent throw
Plus pipe 4135, flocculant concentration pipe 4136,
Water out 4202 is rinsed in continuous sand filter 4200, compressed air inlet 4201, sand filtration.
Embodiment
Embodiment of the present utility model is described below in detail, the example of the embodiment is shown in the drawings, wherein from beginning
Same or similar element or element with same or like function are represented to same or similar label eventually.Below by ginseng
The embodiment for examining accompanying drawing description is exemplary, it is intended to for explaining the utility model, and it is not intended that to the utility model
Limitation.
Below with reference to the accompanying drawings advanced waste treatment system 60 according to the utility model embodiment, Sewage advanced treatment are described
System 60 is used for the finishing operation in the whole technological process of wastewater treatment, further removes the COD remained in water removal.
As depicted in figs. 1 and 2, filled according to the advanced waste treatment system 60 of the utility model embodiment including Fenton's reaction
Put 4100.
Fenton's reaction device 4100 includes Fenton's reaction pond 4110 and the Fenton being sequentially communicated along waste water treatment process direction
Sedimentation basin 4130.There is the Fenton's reaction chamber being sequentially communicated along the waste water treatment process direction in Fenton's reaction pond 4110
4111st, PH adjust back chamber 4115, adsorbent chamber 4116 and Fenton flocculation chamber 4112, wherein, PH readjustment chamber 4115 in PH refer to hydrogen from
Sub- concentration, the acid-base value of ie in solution.Wherein, Fenton's reaction chamber 4111 adds mouth 4121, catalyst with acid and adds the and of mouth 4122
Oxidant adds mouth 4123, and there is PH readjustment chambers 4115 alkali to add mouth 4124, and there is adsorbent chamber 4116 adsorbent to add mouth 4125,
Fenton flocculation chamber 4112 has flocculant concentration mouthful 4126.
In other words, acid adds that mouth 4121, catalyst add mouth 4122 and oxidant adds mouth 4123 and Fenton's reaction chamber
4111 connections, for delivering sour (such as sulfuric acid), catalyst (such as ferrous sulfate) and oxidation to Fenton's reaction chamber 4111 respectively
Agent (such as hydrogen peroxide).Alkali adds mouth 4124 and connected with PH readjustment chambers 4115, for delivering alkali to PH readjustment chambers 4115.Adsorbent
Add mouth 4125 to connect with adsorbent chamber 4116, for adding adsorbent (such as activated carbon) to adsorbent chamber 4116.Flocculant concentration
Mouth 4126 is connected with Fenton flocculation chamber 4112, for delivering flocculant to Fenton flocculation chamber 4112.
Need exist for being appreciated that, acid add mouth 4121, catalyst add mouth 4122, oxidant add mouth 4123, alkali throw
Plus mouth 4124, adsorbent add mouth 4125, flocculant concentration mouth 4126 and can be arranged on Fenton's reaction pond 4110；It can also make
The upper surface in Fenton's reaction pond 4110 is opened wide, and makes acid add mouth 4121, catalyst and add mouth 4122, oxidant to add mouth
4123rd, alkali, which adds mouth 4124, adsorbent and adds mouth 4125, flocculant concentration mouthfuls 4126, is suspended in the top of Fenton's reaction pond 4110.
It will be appreciated by those skilled in the art that ground is, waste water treatment process direction refers to, in whole works of wastewater treatment
In sequence, along the ordering of each operation, waste water is from flow direction of first procedure sequentially into last procedure.
According to the advanced waste treatment system 60 of the utility model embodiment, by setting position in Fenton's reaction pond 4110
The adsorbent chamber 4116 between chamber 4115 and Fenton flocculation chamber 4112 is adjusted back in PH, and is set and absorption on Fenton's reaction pond 4110
The adsorbent that chamber 4116 is connected adds mouth 4125, and absorption is added to adsorbent chamber 4116 so as to add mouth 4125 by adsorbent
COD in agent, such as activated carbon, such waste water is oxidized under certain pH condition after carbon dioxide and water, it is possible to use thrown
Plus adsorbent absorption Fenton's reaction after waste water remain COD, when difficult degradation COD concentration is higher in waste water, still
Processing requirement can be reached, and without subsequently setting such as activated-charcoal column isoreactivity charcoal processing dress in Fenton's reaction device 4100
Put, simplify the structure of advanced waste treatment system 60, and reduce the cost of advanced waste treatment system 60.In addition, adding
Charcoal absorption after the useless charcoal that produces flow into Fenton sedimentation basin 4130, handled together with the chemical sludge that Fenton's reaction is produced,
These sludge can go to burn so as to recovered carbon again, save the cost and manual cleaning activated-charcoal column of activated carbon recovery
Cost.
Therefore, COD high treating effects, structure letter are had according to the advanced waste treatment system 60 of the utility model embodiment
Single, low cost and other advantages.
Below with reference to the accompanying drawings advanced waste treatment system 60 according to the utility model specific embodiment is described.
As depicted in figs. 1 and 2, filled according to the advanced waste treatment system 60 of the utility model embodiment including Fenton's reaction
Put 4100.
In some specific embodiments of the present utility model, as depicted in figs. 1 and 2, provided with the in Fenton's reaction chamber 4111
One Fenton mixer 4113.And/or, Fenton's reaction pond 4110 is provided with the first stirring air connected with Fenton's reaction chamber 4111
Entrance (not shown), is stirred with being passed through air to Fenton's reaction chamber 4111 living.
The second Fenton mixer 4117 is provided with PH readjustment chambers 4115.And/or, Fenton's reaction pond 4110 is provided with to be returned with PH
The second stirring air intake (not shown) that chamber 4115 is connected is adjusted, is stirred with being passed through air to PH readjustment chambers 4115.
The 3rd Fenton mixer 4118 (as shown in Figure 1), turn of the 3rd Fenton mixer 4118 are provided with adsorbent chamber 4116
Speed is higher than the rotating speed of the 4th Fenton mixer 4114.And/or, Fenton's reaction pond 4110 is provided with the connected with adsorbent chamber 4116
Three stirring air intakes 4127 (as shown in Figure 2), are stirred with being passed through air to adsorbent chamber 4116.
The 4th Fenton mixer 4114 is provided with Fenton flocculation chamber 4112.And/or, Fenton's reaction pond 4110 is provided with and sweet smell
The 4th stirring air intake (not shown) that the flocculation chamber 4112 that pauses is connected, to be passed through air progress to Fenton flocculation chamber 4112
Stirring.
Fenton mud scraper 4132 is provided with Fenton sedimentation basin 4130.
In other words, it is each in Fenton's reaction chamber 4111, PH readjustments chamber 4115, adsorbent chamber 4116 and Fenton flocculation chamber 4112
It is individual, can be using mixer stirring, it would however also be possible to employ compressed air is stirred, and mixer and compressed air can also be used simultaneously
Stirring.Wherein, the rotating speed of the first Fenton mixer 4113, the rotating speed of the second Fenton mixer 4117, the 3rd Fenton mixer
4118 rotating speed is respectively higher than the rotating speed of the 4th Fenton mixer 4114,
It is possible thereby to pass through the first Fenton mixer 4113, the second Fenton mixer 4117, the 3rd Fenton mixer 4118
Waste water is stirred with the 4th Fenton mixer 4114, so as to improve abolishment treatment effeciency, and can be gone using Fenton mud scraper 4132
Except the sludge in Fenton sedimentation basin 4130.
Wherein, as shown in figure 1, being provided with Fenton's reaction pond 4110 in the embodiment of the 3rd stirring air intake 4127,
Advanced waste treatment system 60 also includes stirring air delivery pipe 4128, and stirring air delivery pipe 4128 is entered by the 3rd stirring air
Mouth 4127 is stretched into adsorbent chamber 4116, for example, the lower end of stirring air delivery pipe 4128 can extend into the bottom of adsorbent chamber 4116
Portion, so as to improve mixing effect.Certainly, the first stirring air intake, the second stirring air intake, the 4th stirring air intake
Corresponding stirring air delivery pipe can be set.
In some specific examples of the present utility model, as depicted in figs. 1 and 2, adding for thing is added for the ease of various
And the setting and connection of advanced waste treatment system 60, advanced waste treatment system 60 also including acid add pipe 4131, catalysis
Agent, which adds pipe 4132, oxidant and adds pipe 4133, alkali and add pipe 4134, adsorbent, adds pipe 4135 and flocculant concentration pipe
4136。
Acid, which adds pipe 4131 and adds mouth 4121 with acid, to be connected, for conveying sulfuric acid.Catalyst adds pipe 4132 and catalyst
Add mouth 4122 to connect, for conveying ferrous sulfate.Oxidant, which adds pipe 4133 and adds mouth 4123 with oxidant, to be connected, for defeated
Send hydrogen peroxide.Alkali, which adds pipe 4134 and adds mouth 4124 with alkali, to be connected, for conveying alkali.Adsorbent adds pipe 4135 and thrown with adsorbent
Plus mouth 4125 is connected, for adding activated carbon.Flocculant concentration pipe 4136 is connected with flocculant concentration mouthful 4126, for conveying wadding
Solidifying agent.
In some specific embodiments of the present utility model, as depicted in figs. 1 and 2, provided with the in Fenton's reaction pond 4110
One dividing plate 4141, the dividing plate 4143 of second partition 4142 and the 3rd.
First dividing plate 4141 separates Fenton's reaction chamber 4111 and PH readjustment chambers 4115, and second partition 4142 separates PH readjustment chambers
4115 and adsorbent chamber 4116, the 3rd dividing plate 4143 separates adsorbent chamber 4116 and Fenton flocculation chamber 4112.First dividing plate 4141 and
The lower end of three dividing plates 4143 is connected with the bottom wall in Fenton's reaction pond 4110, lower end and the Fenton's reaction pond 4110 of second partition 4142
Bottom wall be spaced apart, and second partition 4142 upper end higher than the first dividing plate 4141 upper end and the 3rd dividing plate 4143 upper end.
Waste water in Fenton's reaction chamber 4111 adjusts back chamber 4115 by the upper end overflow of the first dividing plate 4141 to PH, and PH is adjusted back in chamber 4115
The waste water that waste water is flow in adsorbent chamber 4116, adsorbent chamber 4116 by the lower end of second partition 4142 is by the upper end of the 3rd dividing plate 4143
Overflow to Fenton flocculate chamber 4112.
In some specific examples of the present utility model, as depicted in figs. 1 and 2, advanced waste treatment system 60 also includes
Continuous sand filter 4200.
Continuous sand filter 4200 is connected with Fenton sedimentation basin 4130, and continuous sand filter 4200 has compressed air inlet 4201
Water out 4202 is rinsed with sand filtration, water out 4202 and the Fenton's reaction chamber 4111 or Fenton in Fenton's reaction pond 4110 are rinsed in sand filtration
Sedimentation basin 4130 is connected.The water that Fenton sedimentation basin 4130 flows out enters continuous sand filter 4200, and compressed air is entered by compressed air
Mouth 4201 enters continuous sand filter 4200 to carry out filter sand to the water in continuous sand filter 4200, and the solid gone in water removal suspends
Thing, improves the degree of purity of the water of outflow, and sand filtration flushing water rinses water out 4202 by sand filtration and returns to Fenton's reaction pond 4110
Fenton's reaction chamber 4111 or Fenton sedimentation basin 4130.
According to the advanced waste treatment system 60 of the utility model embodiment, mouth 4125 is added to adsorbent chamber by adsorbent
4116 add activated carbon, it is possible to use the COD that waste water is remained after the charcoal absorption Fenton's reaction added, and without anti-in Fenton
Answer device 4100 that such as activated-charcoal column isoreactivity charcoal processing unit is subsequently set, simplify the knot of advanced waste treatment system 60
Structure, and reduce the cost of advanced waste treatment system 60.In addition, the activated carbon added is recyclable, activated carbon recovery is saved
Cost and manual cleaning activated-charcoal column cost.
In description of the present utility model, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", " on ", " under ", "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom " " interior ", " outer ", " suitable
The orientation or position relationship of the instruction such as hour hands ", " counterclockwise " are based on orientation shown in the drawings or position relationship, merely to just
Described in description the utility model with simplified, rather than indicate or imply that the device or element of meaning must be with specific sides
Position, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.
In addition, term " first ", " second " are only used for describing purpose, and it is not intended that indicating or implying relative importance
Or the implicit quantity for indicating indicated technical characteristic.Thus, define " first ", the feature of " second " can express or
Implicitly include one or more this feature.In description of the present utility model, " multiple " are meant that at least two, example
Such as two, three etc., unless otherwise specifically defined.
In the utility model, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " Gu
It is fixed " etc. term should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integrally；Can be
Mechanically connect or electrically connect；Can be joined directly together, can also be indirectly connected to by intermediary, can be two
The connection of element internal or the interaction relationship of two elements.For the ordinary skill in the art, can basis
Concrete condition understands concrete meaning of the above-mentioned term in the utility model.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature it " on " or it
" under " can directly be contacted including the first and second features, it is not direct contact but logical that can also include the first and second features
The other characterisation contact crossed between them.Moreover, fisrt feature second feature " on ", " top " and " above " include the
One feature is directly over second feature and oblique upper, or is merely representative of fisrt feature level height higher than second feature.First is special
Levy second feature " under ", " lower section " and " below " include fisrt feature immediately below second feature and obliquely downward, or only
Represent that fisrt feature level height is less than second feature.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means to combine specific features, structure, material or the spy that the embodiment or example are described
Point is contained at least one embodiment of the present utility model or example.In this manual, to the schematic table of above-mentioned term
State and be necessarily directed to identical embodiment or example.Moreover, specific features, structure, material or the feature of description can be with
Combined in an appropriate manner in any one or more embodiments or example.In addition, those skilled in the art can be by
Not be the same as Example or example described in this specification are engaged and combined.
Although embodiment of the present utility model has been shown and described above, it is to be understood that above-described embodiment is
Exemplary, it is impossible to it is interpreted as to limitation of the present utility model, one of ordinary skill in the art is in scope of the present utility model
It is interior above-described embodiment to be changed, changed, replaced and modification.
Claims (10)
1. a kind of advanced waste treatment system, it is characterised in that including：
Fenton's reaction device, the Fenton's reaction device includes having along waste water in Fenton's reaction pond, the Fenton's reaction pond
Fenton's reaction chamber, PH readjustments chamber, adsorbent chamber and Fenton flocculation chamber that reason process orientation is sequentially communicated；
There is the Fenton's reaction chamber acid to add, and mouth, catalyst add mouth and oxidant adds mouth；
There is the PH readjustments chamber alkali to add mouth；
There is the adsorbent chamber adsorbent to add mouth；
The Fenton flocculation chamber has flocculant concentration mouthful.
2. advanced waste treatment system according to claim 1, it is characterised in that the Fenton's reaction pond is provided with and institute
State the first stirring air intake of Fenton's reaction chamber connection；And/or
The Fenton's reaction intracavitary is provided with the first Fenton mixer.
3. advanced waste treatment system according to claim 1, it is characterised in that the Fenton's reaction pond is provided with and institute
State the second stirring air intake of PH readjustment chamber connections；And/or
The PH readjustments intracavitary is provided with the second Fenton mixer.
4. advanced waste treatment system according to claim 1, it is characterised in that the Fenton's reaction pond is provided with and institute
State the 3rd stirring air intake of adsorbent chamber connection；And/or
The 3rd Fenton mixer is provided with the adsorbent chamber.
5. advanced waste treatment system according to claim 4, it is characterised in that the Fenton's reaction pond is provided with and institute
The 3rd stirring air intake of adsorbent chamber connection is stated, the advanced waste treatment system also includes：
Air delivery pipe is stirred, the stirring air delivery pipe is stretched into the adsorbent chamber by the described 3rd stirring air intake.
6. advanced waste treatment system according to claim 1, it is characterised in that the Fenton flocculation intracavitary is provided with the 4th
Fenton mixer；And/or
The Fenton's reaction pond is provided with the 4th stirring air intake connected with Fenton flocculation chamber.
7. the advanced waste treatment system according to any one of claim 1-6, it is characterised in that also include：
Acid adds pipe, and the acid, which adds pipe and adds mouth with the acid, to be connected；
Catalyst adds pipe, and the catalyst, which adds pipe and adds mouth with the catalyst, to be connected；
Oxidant adds pipe, and the oxidant, which adds pipe and adds mouth with the oxidant, to be connected；
Alkali adds pipe, and the alkali, which adds pipe and adds mouth with the alkali, to be connected；
Adsorbent adds pipe, and the adsorbent, which adds pipe and adds mouth with the adsorbent, to be connected；
Flocculant concentration pipe, the flocculant concentration pipe is connected with the flocculant concentration mouthful.
8. the advanced waste treatment system according to any one of claim 1-6, it is characterised in that the Fenton's reaction pond
It is interior to adjust back chamber and the adsorbent chamber provided with the first dividing plate, the separation PH that separate the Fenton's reaction chamber and PH readjustment chambers
Second partition and separate the adsorbent chamber and the Fenton and flocculate the 3rd dividing plate of chamber, first dividing plate and the described 3rd every
The lower end of plate is connected with the bottom wall in the Fenton's reaction pond, between the bottom wall in the lower end of the second partition and the Fenton's reaction pond
Separate and upper end is higher than the upper end of first dividing plate and the upper end of the 3rd dividing plate.
9. the advanced waste treatment system according to any one of claim 1-6, it is characterised in that the Fenton's reaction dress
Putting also includes Fenton sedimentation basin, and the Fenton's reaction pond connects successively with the Fenton sedimentation basin along the waste water treatment process direction
It is logical.
10. advanced waste treatment system according to claim 9, it is characterised in that also include：
Continuous sand filter, the continuous sand filter is connected with the Fenton sedimentation basin, and the continuous filter sand utensil has compressed air
Water out is rinsed in import and sand filtration, and water out and the Fenton's reaction chamber or the Fenton in the Fenton's reaction pond are rinsed in the sand filtration
Sedimentation basin is connected.
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| CN201621460296.6U CN206417935U (en) | 2016-12-28 | 2016-12-28 | Advanced waste treatment system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108249612A (en) * | 2016-12-28 | 2018-07-06 | 帕克环保技术(上海)有限公司 | Advanced waste treatment system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108249612A (en) * | 2016-12-28 | 2018-07-06 | 帕克环保技术(上海)有限公司 | Advanced waste treatment system |
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