CN206435206U - One kind reinforcing Fenton's reaction mixes equipment - Google Patents

One kind reinforcing Fenton's reaction mixes equipment Download PDF

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Publication number
CN206435206U
CN206435206U CN201720055208.2U CN201720055208U CN206435206U CN 206435206 U CN206435206 U CN 206435206U CN 201720055208 U CN201720055208 U CN 201720055208U CN 206435206 U CN206435206 U CN 206435206U
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China
Prior art keywords
stirring
fenton
agitating shaft
reaction mixes
reaction
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CN201720055208.2U
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Chinese (zh)
Inventor
周健
王磊
李星桥
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Suzhou Zhanqing Environment Protection Technology Co Ltd
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Suzhou Zhanqing Environment Protection Technology Co Ltd
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Abstract

One kind reinforcing Fenton's reaction mixes equipment, including cavity, water inlet is arranged at the bottom of cavity, delivery port is arranged at top, there is vertical agitator inside, the agitator includes agitating shaft, it is arranged on the stirring cylinder of coaxial line and the stirring blade for the staggeredly hollow out for being arranged on stirring cylinder outer surface on agitating shaft, the utility model is using the agitator type optimized, mixing tool provides the ability of radial shear power and normal direction shearing force simultaneously, in high-speed stirred, enabling in reactor waste water, diametrically (section) obtains stronger mixed effect, the blade form that the utility model agitator is interspersed, releasable axle upwards pressure, reduce axially upper mixed flow and the phenomenon of back mixing, ideal piston flow is presented when making waste water by reactor.

Description

One kind reinforcing Fenton's reaction mixes equipment
Technical field
The utility model belongs to technical field of waste water processing, and more particularly to a kind of reinforcing Fenton's reaction mixes equipment.
Background technology
In the last few years, what Fenton's reaction was applied in the treatment of waste water is more and more extensive.Fenton's reaction is by French scientist The reaction that Fenton was found in 1894.Fenton's reaction is in acid condition, to pass through Fe2+It is catalyzed H2O2, inspire with strong oxygen The hydroxyl radical free radical for the property changed, and then further occur subsequent chemical reaction.Fenton's reaction has extensively in field of waste water treatment Use.The hydroxyl radical free radical that Fenton's reaction is inspired, quickly can be aoxidized organic matter contained in waste water.Fenton Most of larger molecular organicses can be oxidized to small organic molecule by reaction, and most of small organic molecule is oxidized into dioxy Change carbon and water.Fenton's reaction can greatly improve the biodegradability of waste water, and being also used as advanced treating of waste water etc., each gives up Water treatment field.Meanwhile, the raw material price needed for Fenton's reaction is cheap, and buying is easy, therefore is obtained extensively in wastewater treatment industry General use.
, it is necessary to be stirred, to strengthen Fe during Fenton's reaction progress2+With H2O2Mixing.Because Fenton's reaction is profit Oxidation reaction is carried out with hydroxyl radical free radical, and the life-span of hydroxyl radical free radical is extremely short, in the life span of hydroxyl radical free radical If not reaching pollutant, hydroxyl radical free radical waste is will result in, therefore, in Fenton's reaction equipment, stirring mass transfer is unusual It is crucial, important.Strong stirring, can strengthen Fe2+With H2O2With the mixing mass transfer of waste water, increase hydroxyl radical free radical and pollutant Contact probability, accelerate Fenton's reaction oxidized waste water in organic matter oxidation rate.Stirring in conventional Fenton's reaction equipment Device is that motor drives an agitating paddle to be stirred.Agitating paddle shape is often two blades or three-vaned individual layer or double-deck stirring Oar, material is often stainless steel.Such a agitating paddle shape is relatively simple, and stirring mass-transfer efficiency is relatively low, and capacity usage ratio is not high.Reach Under the target stirred, the electrode power of selection is larger, causes power consumption higher.
The content of the invention
In order to overcome the above-mentioned equipment of Fenton's reaction in the prior art stirring mass-transfer efficiency relatively low, oxidation rate is slower, energy consumption Serious, elapsed time is long, and the clearance for the Organic substance in water that gives up is low, the shortcomings of causing discharge beyond standards, the purpose of this utility model It is that providing a kind of reinforcing Fenton's reaction mixes equipment, mixing is strong, and reaction effect is good.
To achieve these goals, the technical solution adopted in the utility model is:
One kind reinforcing Fenton's reaction mixes equipment, including cavity 2, and water inlet 1 is arranged at the bottom of cavity 2, and top has There is a vertical agitator mouth of a river 6, inside, and the agitator includes agitating shaft 4, is arranged on stirring for coaxial line on agitating shaft 4 Mix cylinder 8 and be arranged on the stirring blade 3 of the staggeredly hollow out of stirring cylinder 8 outer surface.
The lower end of the agitating shaft 4 is arranged in the blender base 7 of the bottom of cavity 2, and upper end is by shaft coupling with slowing down The output connection of motor 5.
The stirring cylinder 8 is enclosed on agitating shaft 4, is connected by way of welding or pin.
The stirring blade 3 has 3~6, by welding or screw fixed form, is circumferentially uniformly arranged on stirring cylinder On 8 wall.
The stirring blade 3 is perpendicular to the stirring tangent line of cylinder 8.
Uniform concavo-convex interphase structure is presented in the stirring blade 3 in the longitudinal direction, and recessed portion is openwork part 9, It is non-openwork part 10 at lower concave part tap agitating shaft 4, projection carries out hollow out, including openwork part 9 and remote agitating shaft 4 Non- openwork part 10, the adjacent area of openwork part 9 and shape be equal, the adjacent area of non-openwork part 10 and shape phase Deng.The radius of the stirring cylinder 8 is 2 with the ratio of the outermost radical length of blade 3 is stirred:1 to 4:1.
The radical length ratio of the hollow-out parts 10 and non-hollow-out parts 9 is 0.5:1 to 2:1.
Stirring blade 3 main body is frame blade shape.
Compared with prior art, the utility model is using the agitator type of optimization, and mixing tool simultaneously radially cut by offer The ability of shear force and normal direction shearing force, in high-speed stirred, enabling in reactor waste water, diametrically (section) is obtained more Strong mixed effect.
The blade form that the utility model agitator is interspersed, releasable axle upwards pressure, and reduces axially upper mixed flow With the phenomenon of back mixing, ideal piston flow is presented when making waste water by reactor.
Brief description of the drawings
Fig. 1 is the utility model structural representation (sectional view).
Fig. 2 is the utility model structural representation (axonometric drawing).
Fig. 3 is the utility model stirring blade structural schematic diagram.
Embodiment
Describe embodiment of the present utility model in detail with reference to the accompanying drawings and examples.
As depicted in figs. 1 and 2, a kind of reinforcing Fenton's reaction mixes equipment, including cavity 2, the bottom of cavity 2 have into Delivery port 6 arranged at the mouth of a river 1, top, and there is a vertical agitator inside, and agitator includes agitating shaft 4, stirring cylinder 8 and staggeredly hollow out Stirring blade 3.
Wherein, the lower end of agitating shaft 4 is arranged in the blender base 7 of the bottom of cavity 2, and upper end is by shaft coupling with slowing down The output connection of motor 5, reducing motor 5 is located at reactor head, the stirring in reactor is imparted power to by shaft coupling Device 4.
Stirring cylinder 8 is enclosed on agitating shaft 4, and the two coaxial line is connected by way of welding or pin.Stirring blade 3 has 3~ 6, by welding or screw fixed form, on the wall for being circumferentially uniformly arranged on stirring cylinder 8, with the stirring tangent line of cylinder 8 Vertically.
As shown in figure 3, uniform concavo-convex interphase structure is presented in the stirring blade 3 in the longitudinal direction, recessed portion is Openwork part 9, the bottom of recessed portion is non-openwork part 10, and projection carries out hollow out, including openwork part 9 and non-hollow out Part 10.
It is 2 to stir the radius of cylinder 8 and the ratio of the stirring outermost radical length of blade 3:1 to 4:1.Hollow-out parts 10 with The radical length ratio of non-hollow-out parts 9 is 0.5:1 to 2:1.
According to above structure, waste water enters from the water inlet 1 of bottom, in cavity by high-speed stirred agitator shearing and Mixing, flows out after reactor from delivery port 6.
Because the stirring main body of blade 3 is frame blade shape, so there is provided the shearing force of radial direction;Engraved again because it is used Empty structure, rotation when, part water flows away from hollow out, therefore there is more strong tangential shearing force.Therefore, agitator There is the ability for providing tangential shearing force and radial shear power simultaneously on section.
Overall stirring blade 3 is frame mode there is provided centrifugal force, from blade inboard water can be thrown into outside, staggeredly The blade form of distribution, result in actually adjacent two blades and different centrifugal force is directly presented, water velocity is inconsistent, enters And adjacent fluid pressure is different, final release shaft upwards pressure, and reduces mixed flow and back mixing phenomenon in a wide range of, leads to waste water Ideal piston flow is presented when crossing reactor.

Claims (8)

1. one kind reinforcing Fenton's reaction mixes equipment, including cavity (2), water inlet (1), top are arranged at the bottom of cavity (2) There is delivery port (6), there is vertical agitator inside, it is characterised in that the agitator includes agitating shaft (4), is arranged on stirring On axle (4) the stirring cylinder (8) of coaxial line and be arranged on stirring cylinder (8) outer surface staggeredly hollow out stirring blade (3)。
2. reinforcing Fenton's reaction mixes equipment according to claim 1, it is characterised in that under the agitating shaft (4) End is arranged in the blender base (7) of cavity (2) bottom, and upper end is connected by shaft coupling with the output of reducing motor (5).
3. reinforcing Fenton's reaction mixes equipment according to claim 1, it is characterised in that stirring cylinder (8) set On agitating shaft (4), it is connected by way of welding or pin.
4. reinforcing Fenton's reaction mixes equipment according to claim 1, it is characterised in that the stirring blade (3) has 3 ~6, by welding or screw fixed form, on the wall for being circumferentially uniformly arranged on stirring cylinder (8).
5. reinforcing Fenton's reaction mixes equipment according to claim 1, it is characterised in that the stirring blade (3) is hung down Directly in stirring cylinder (8) tangent line.
6. reinforcing Fenton's reaction mixes equipment according to claim 5, it is characterised in that the stirring blade (3) exists Uniform concavo-convex interphase structure is presented on length direction, recessed portion is openwork part (9), and the bottom of recessed portion connects agitating shaft (4) place is non-openwork part (10), and projection carries out hollow out, including openwork part (9) and the non-hollow out away from agitating shaft (4) Partly (10).
7. reinforcing Fenton's reaction mixes equipment according to claim 6, it is characterised in that the stirring cylinder (8) The ratio of radius and stirring blade (3) outermost radical length is 2:1 to 4:1.
8. according to claim 6 reinforcing Fenton's reaction mix equipment, it is characterised in that the hollow-out parts (10) with it is non- The radical length ratio of hollow-out parts (9) is 0.5:1 to 2:1.
CN201720055208.2U 2017-01-16 2017-01-16 One kind reinforcing Fenton's reaction mixes equipment Active CN206435206U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720055208.2U CN206435206U (en) 2017-01-16 2017-01-16 One kind reinforcing Fenton's reaction mixes equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720055208.2U CN206435206U (en) 2017-01-16 2017-01-16 One kind reinforcing Fenton's reaction mixes equipment

Publications (1)

Publication Number Publication Date
CN206435206U true CN206435206U (en) 2017-08-25

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720055208.2U Active CN206435206U (en) 2017-01-16 2017-01-16 One kind reinforcing Fenton's reaction mixes equipment

Country Status (1)

Country Link
CN (1) CN206435206U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111470588A (en) * 2020-03-20 2020-07-31 厦门绿动力环境治理工程有限公司 High concentration waste water reduction electro-Fenton tank structure convenient to dismouting is washd

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111470588A (en) * 2020-03-20 2020-07-31 厦门绿动力环境治理工程有限公司 High concentration waste water reduction electro-Fenton tank structure convenient to dismouting is washd

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