CN207276283U - A kind of Fenton oxidation pilot plant of novel integrated - Google Patents
A kind of Fenton oxidation pilot plant of novel integrated Download PDFInfo
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- CN207276283U CN207276283U CN201720986174.9U CN201720986174U CN207276283U CN 207276283 U CN207276283 U CN 207276283U CN 201720986174 U CN201720986174 U CN 201720986174U CN 207276283 U CN207276283 U CN 207276283U
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- fenton
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- dosing pump
- pump
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Abstract
A kind of Fenton oxidation pilot plant of novel integrated；Including rack, Fenton's reaction groove, water feed apparatus, discharging device and chemicals dosing plant；Water feed apparatus includes water inlet pipe and intake pump；Water inlet pipe is connected with intake pump and is arranged on the side of Fenton's reaction groove；Discharging device includes multistage exhaust outlet, and multistage exhaust outlet includes outlet pipe, overflow pipe and blow-down pipe；Outlet pipe is a plurality of, is successively set on the opposite side of Fenton's reaction groove；Blow-down pipe is also to be a plurality of, and this plurality of blow-down pipe is connected with overflow pipe；Chemicals dosing plant includes the dosing tank for being arranged on Fenton's reaction groove top, and the dosing pump to connect one to one with dosing tank.The utility model carries multistage exhaust outlet, according to the water flow of multistage exhaust outlet, can flexibly adjust and timely control each reaction time, reach the volume using reaction tank of maximal efficiency.
Description
Technical field
The utility model belongs to pressure vessel industrial wastewater and sanitary sewage disposal technical field, is related to a kind of new integrated
The Fenton oxidation pilot plant of change.
Background technology
Fenton reactor is the equipment being commonly used in sewage disposal, for removing the organic pollution of difficult degradation, now
Fenton reactor mainly realize that medicine mixes by stirring, in this process, add power consumption, medicine mixing
Effect is uneven, and the invalid of medicine utilizes increase, so as to cause reaction efficiency to reduce.
Hydrogen peroxide（H2O2）With hydroxyl radical free radical of the ferrous ion reaction generation with Strong oxdiative ability, will can hold
Long property organic matter, particularly common reagent are difficult to the aromatic compounds and some heterocycle compounds aoxidized, in Fenton
（Fenton）All decomposed in face of reagent by no selective oxidation.Fenton（Fenton）Reagent is a kind of common advanced oxidation skill
Art, for other oxidants, it just can destroy organic matter in the dark, have that operating process is simple, reaction is easy to get, runs
Of low cost, equipment investment is few and the advantages that environmentally friendly property.Although above-mentioned processing method generally uses, still suffer from
Some shortcomings, are mainly manifested in：The labor intensity of Fenton processing is big, of high cost, and sludge is more, waste water easily returns color, medicament operation
Parameter is difficult to control and medicament corrosivity is stronger etc..
Therefore, how to solve the above problems, be the content to be studied of those skilled in the art.
The content of the invention
To overcome above-mentioned deficiency of the prior art, the utility model aim in offer in it can solve current Fenton
Try a kind of Fenton oxidation pilot plant of the novel integrated for the problems such as equipment volume is larger, sludge yield is big.
In order to achieve the above objects and other related objects, the utility model is provided in a kind of Fenton oxidation of novel integrated
Try equipment；Including rack, Fenton's reaction groove, water feed apparatus, discharging device and chemicals dosing plant；The water feed apparatus includes water inlet pipe
And intake pump；The water inlet pipe is connected with the intake pump and is arranged on the side of the Fenton's reaction groove；The water outlet dress
Put includes outlet pipe, overflow pipe and blow-down pipe including multistage exhaust outlet, the multistage exhaust outlet；The outlet pipe is plural number
It is a, it is successively set on the opposite side of the Fenton's reaction groove；The blow-down pipe is also to be a plurality of, and this plurality of blow-down pipe is equal
Connected with the overflow pipe；The chemicals dosing plant includes a plurality of dosing tanks for being arranged on the Fenton's reaction groove top, and
The dosing pump to connect one to one with a plurality of dosing tanks.
In above-mentioned technical proposal, related content is explained as follows：
1st, in such scheme, electric cabinet is further included；The electric cabinet is also disposed at the lower section of the rack；The water inlet
Pump, dosing pump are electrically connected with the electric cabinet.
2nd, in such scheme, PLC display screens is additionally provided with the lateral surface of the Fenton's reaction groove and PLC automatically controls frequency conversion
Device, the PLC display screens and PLC automatically control frequency converter and are electrically connected with the electric cabinet.
3rd, in such scheme, the dosing pump includes sulfuric acid/liquid caustic soda dosing pump, hydrogen peroxide dosing pump and ferrous sulfate dosing
Pump；Sulfuric acid/liquid caustic soda dosing pump, hydrogen peroxide dosing pump and ferrous sulfate dosing pump described in this are successively set under the rack
Side.
4th, in such scheme, the sulfuric acid/liquid caustic soda dosing pump, hydrogen peroxide dosing pump and ferrous sulfate dosing pump are accurate
Measure peristaltic pump.The accurate measurement peristaltic pump can be with automatic feeding, and records the dosage of accumulation.
5th, in such scheme, the bottom of the rack is equipped with adjustment foot.
Since above-mentioned technical proposal is used, the utility model this have the advantage that compared with prior art：
The utility model carries multistage exhaust outlet, according to the water flow of multistage exhaust outlet, can flexibly adjust
And each reaction time is timely controlled, reach the volume using reaction tank of maximal efficiency.The setting of foundation multistage discharging device,
Each section of variation of water can be monitored in real time, Statistical reference, more water process are provided to tackle the mutation of water quality condition
The good operation of equipment provides basic data and supports.And provide can for the effect for the being arranged to medicament detection of multistage exhaust outlet
Can, it can follow up and judge the situation of change of each stage dose efficacy, be the addition of medicament and the change of dosage
Actual reference is provided.
Brief description of the drawings
Fig. 1 is the utility model structure diagram；
Fig. 2 is the utility model structure diagram two；
Fig. 3 is A in Fig. 2 to structure diagram.
Embodiment
Illustrate the embodiment of the utility model by particular specific embodiment below, those skilled in the art can be by this
Content disclosed by specification understands other advantages and effect of the utility model easily.
Please refer to Fig.1 to Fig.3.It should be clear that structure, ratio, size depicted in this specification institute accompanying drawings etc., only to
Coordinate the revealed content of specification, so that those skilled in the art understands and reads, be not limited to the utility model
Enforceable qualifications, therefore do not have technical essential meaning, the modification of any structure, the change of proportionate relationship or size
Adjustment, in the case where not influencing the effect of the utility model can be generated and the purpose that can reach, should all still fall in the utility model
Revealed technology contents are obtained in the range of covering.Meanwhile in this specification it is cited as " on ", " under ", " left side ",
The term on " right side ", " centre " and " one " etc., is merely convenient to understanding for narration, and it is enforceable to be not used to restriction the utility model
Scope, its relativeness are altered or modified, enforceable when being also considered as the utility model in the case where changing technology contents without essence
Category.
As shown in Figure 1 to Figure 3, the Fenton oxidation pilot plant of a kind of novel integrated；Including rack 1, Fenton's reaction groove
2nd, water feed apparatus, discharging device and chemicals dosing plant；The water feed apparatus includes water inlet pipe 3 and intake pump 4；The water inlet pipe 3 with
The intake pump 4 is connected and is arranged on the side of the Fenton's reaction groove 2；The discharging device includes multistage exhaust outlet,
The multistage exhaust outlet includes outlet pipe 5, overflow pipe 6 and blow-down pipe 7；The outlet pipe 5 is a plurality of, is successively set on institute
On the opposite side for stating Fenton's reaction groove 2；The blow-down pipe 7 also to be a plurality of, and this plurality of blow-down pipe 7 with the overflow pipe
6 connections；The chemicals dosing plant includes being arranged on a plurality of dosing tanks 8 on 2 top of Fenton's reaction groove, and with a plurality of institutes
State the dosing pump that dosing tank 8 connects one to one.
Further include electric cabinet 9；The electric cabinet 9 is also disposed at the lower section of the rack 1；The intake pump 4, dosing pump with
The electric cabinet 9 is electrically connected.
PLC display screens 10 are additionally provided with the lateral surface of the Fenton's reaction groove 2 and PLC automatically controls frequency converter（In figure not
Show）, the PLC display screens 10 and PLC automatically control frequency converter and are electrically connected with the electric cabinet 9.
The dosing pump includes sulfuric acid/liquid caustic soda dosing pump 11, hydrogen peroxide dosing pump 12 and ferrous sulfate dosing pump 13；This institute
The sulfuric acid stated/liquid caustic soda dosing pump 11, hydrogen peroxide dosing pump 12 and ferrous sulfate dosing pump 13 are successively set under the rack 1
Side.
The sulfuric acid/liquid caustic soda dosing pump 11, hydrogen peroxide dosing pump 12 and ferrous sulfate dosing pump 13 are that accurate measurement is compacted
Dynamic pump.The accurate measurement peristaltic pump can be with automatic feeding, and records the dosage of accumulation.
The bottom of the rack 1 is equipped with adjustment foot 14.
The utility model carries multistage exhaust outlet, according to the water flow of multistage exhaust outlet, can flexibly adjust
And each reaction time is timely controlled, reach the volume using reaction tank of maximal efficiency.The setting of foundation multistage discharging device,
Each section of variation of water can be monitored in real time, Statistical reference, more water process are provided to tackle the mutation of water quality condition
The good operation of equipment provides basic data and supports.And provide can for the effect for the being arranged to medicament detection of multistage exhaust outlet
Can, it can follow up and judge the situation of change of each stage dose efficacy, be the addition of medicament and the change of dosage
Actual reference is provided.
The above embodiments are only illustrative of the principle and efficacy of the utility model, new not for this practicality is limited
Type.Any person skilled in the art can all carry out above-described embodiment under the spirit and scope without prejudice to the utility model
Modifications and changes.Therefore, such as those of ordinary skill in the art without departing from the revealed essence of the utility model
God and all equivalent modifications completed under technological thought or change, should be covered by the claim of the utility model.
Claims (6)
- A kind of 1. Fenton oxidation pilot plant of novel integrated；It is characterized in that：Including rack, Fenton's reaction groove, water inlet dress Put, discharging device and chemicals dosing plant；The water feed apparatus includes water inlet pipe and intake pump；The water inlet pipe connects with the intake pump Lead to and be arranged on the side of the Fenton's reaction groove；The discharging device includes multistage exhaust outlet, and the multistage gives off Mouth includes outlet pipe, overflow pipe and blow-down pipe；The outlet pipe is a plurality of, is successively set on the another of the Fenton's reaction groove On side；The blow-down pipe is also to be a plurality of, and this plurality of blow-down pipe is connected with the overflow pipe；The chemicals dosing plant includes A plurality of dosing tanks on the Fenton's reaction groove top are arranged on, and are added with what a plurality of dosing tanks connected one to one Teat pipette.
- 2. the Fenton oxidation pilot plant of novel integrated according to claim 1, it is characterised in that：Further include automatically controlled Case；The electric cabinet is also disposed at the lower section of the rack；The intake pump, dosing pump are electrically connected with the electric cabinet.
- 3. the Fenton oxidation pilot plant of novel integrated according to claim 1, it is characterised in that：The Fenton's reaction PLC display screens are additionally provided with the lateral surface of groove and PLC automatically controls frequency converter.
- 4. the Fenton oxidation pilot plant of novel integrated according to claim 1, it is characterised in that：The dosing pump bag Include sulfuric acid/liquid caustic soda dosing pump, hydrogen peroxide dosing pump and ferrous sulfate dosing pump；Sulfuric acid/liquid caustic soda dosing pump, hydrogen peroxide described in this Dosing pump and ferrous sulfate dosing pump are successively set on the lower section of the rack.
- 5. the Fenton oxidation pilot plant of novel integrated according to claim 4, it is characterised in that：Sulfuric acid/the liquid Alkali dosing pump, hydrogen peroxide dosing pump and ferrous sulfate dosing pump are accurate measurement peristaltic pump.
- 6. the Fenton oxidation pilot plant of novel integrated according to claim 1, it is characterised in that：The bottom of the rack Portion is equipped with adjustment foot.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720986174.9U CN207276283U (en) | 2017-08-08 | 2017-08-08 | A kind of Fenton oxidation pilot plant of novel integrated |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720986174.9U CN207276283U (en) | 2017-08-08 | 2017-08-08 | A kind of Fenton oxidation pilot plant of novel integrated |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207276283U true CN207276283U (en) | 2018-04-27 |
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ID=61987042
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720986174.9U Active CN207276283U (en) | 2017-08-08 | 2017-08-08 | A kind of Fenton oxidation pilot plant of novel integrated |
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| Country | Link |
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| CN (1) | CN207276283U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114735840A (en) * | 2022-02-28 | 2022-07-12 | 深圳双瑞环保能源科技有限公司 | Visual fenton reaction system |
-
2017
- 2017-08-08 CN CN201720986174.9U patent/CN207276283U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114735840A (en) * | 2022-02-28 | 2022-07-12 | 深圳双瑞环保能源科技有限公司 | Visual fenton reaction system |
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