CN2934215Y - Integral reactor - Google Patents
Integral reactor Download PDFInfo
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- CN2934215Y CN2934215Y CN 200620091451 CN200620091451U CN2934215Y CN 2934215 Y CN2934215 Y CN 2934215Y CN 200620091451 CN200620091451 CN 200620091451 CN 200620091451 U CN200620091451 U CN 200620091451U CN 2934215 Y CN2934215 Y CN 2934215Y
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- main reaction
- integral reactor
- water
- reactor according
- reaction pond
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Abstract
An integral reactor relates to a sanitary-treating arrangement comprising a main reaction pool, a base, a PH regulating device and a PH detecting device. The base is arranged with a stabilized voltage power supply, a set of mixing equipment, an indicator and an aerator. The PH value regulating device is provided at the top of the main reaction pool. The PH value detecting device is provided inside the main reaction pool. The device can be used dynamically and statically in project and test. The requirements of water project and test can be fulfilled via the selection of size of the reactor and electrodes of different pairs according to the water quantity and water quality. The device can display and test current density, PH and mixing intensity. Then, the treatment of water with different qualities can be fulfilled through direct or indirect change of various factors.
Description
Technical field
The utility model relates to a kind of waste disposal plant, particularly relates to a kind of integral reactor.
Background technology
Along with developing rapidly of industry such as petrochemical complex, medicine, agricultural chemicals and fuel, the quantity of biodegradable organic compounds and kind and day sharp increase in the waste water, its harm is serious day by day, has become the focal issue of water pollution control.In order to realize that the organism in the water is effectively decomposed, arise at the historic moment based on the high-level oxidation technology that produces hydroxyl radical free radical (OH).
In China, utilizing electrolysis process that used water difficult to degradate is handled progressively carries out, electricity-Fenton (Fenton) method is emerging a kind of electrolysis process recent years, in engineering of water treatment, use to some extent, but this technology does not have integrated device and the teaching demonstration and the trial model of moulding in each engineering of water treatment and laboratory.Integrated operation and the operational management relative complex of getting up.Thereby delayed the further application of this method in engineering to a certain extent.
The drawback of traditional electrical-Fenton (Fenton) method in wastewater treatment:
1. traditional electrical-Fenton (Fenton) method is handled used water difficult to degradate because of relating to various reaction factors, debugging and control reaction conditions are very inconvenient, and each equipment that reacts required all is independently, do not have the integrated apparatus of moulding, complicated operation is unfavorable for management in actual applications.Both waste manpower and materials, wasted resource again.
2. tradition answers electricity consumption-Fenton (Fenton) method to handle organic wastewater with difficult degradation thereby because of there not being the integrated apparatus of moulding, in practical engineering application, suitable indifferent to waste water quality can not change various factors at any time according to practical situation, and it often is not very desirable causing treatment effect.
3. it is higher to use traditional electrical-Fenton (Fenton) method removal waste water cost.
Summary of the invention
The purpose of this utility model is to provide a kind of waste disposal plant that develops by change and coupling to reaction conditions on the basis of traditional F enton (Fenton) method, this integrated apparatus all concentrates on voltage stabilized source, whipping device, indicating instrument, aerator on the base, pH regulator equipment is placed side top, main reaction pond, make the complete assembly compact construction, easy to use, can according to handle the water yield and water quality situation voluntarily the selecting reactor size satisfy water conservancy project journey and test requirements document with different right electrodes.
The purpose of this utility model is achieved through the following technical solutions:
Integral reactor comprises main reaction pond, base, pH regulator equipment and pH means of detection; Described base is provided with voltage stabilized source, whipping device, indicating instrument, aerator, and pH regulator equipment places side top, main reaction pond, and the pH means of detection places inside, main reaction pond.
Aforesaid whipping device is the rotor that is located at bottom, main reaction pond.
Aforesaid indicating instrument comprises pH value display instrument, stirring intensity display instrument and strength of current display instrument.
Aforesaid aerator comprises gas meter and aeration head.
Aforesaid pH regulator equipment is the soda acid storage device that is provided with acid-adding port, adds the alkali mouth.
Aforesaid pH means of detection is the pH probe.
Aforesaid main reaction is provided with cathode plate and plate in the pond.
Advantage of the present utility model and effect are:
1. the utility model is provided with strength of current display instrument, pH display instrument, stirring intensity display instrument and corresponding adjusting knob, can realize the demonstration directly perceived and the debugging of current density, pH value, stirring intensity.By direct or indirect change various factors, reach the water treatment situation that adapts to different quality.
2. the utility model all concentrates on voltage stabilized source, whipping device, indicating instrument, aerator on the base, and pH regulator equipment is placed side top, main reaction pond, makes complete assembly structurally very compact, uses also very convenient.
3. whole device of the present utility model is after feeding waste water, and only needing easily to start each button is the purpose that the achievable pair organic wastewater with difficult degradation thereby is handled.
Description of drawings
Fig. 1 is an one-piece construction synoptic diagram of the present utility model;
Fig. 2 is a front view of the present utility model;
Fig. 3 is a left view of the present utility model;
Fig. 4 is a vertical view of the present utility model;
Fig. 5 is a process flow sheet of the present utility model.
Embodiment
With reference to the accompanying drawings the utility model is elaborated.
With iron anode, graphite cathode is example
As shown in the figure, the utility model comprises main reaction pond, base, pH regulator equipment and pH means of detection.Integrated equipment such as voltage stabilized source, whipping device, indicating instrument, aerator on the base 8 wherein.
After sewage enters reaction tank by water-in 17, at first by be located at soda acid by the acid-adding port on the soda acid storage device 12, add alkali mouth 3 and come the required pH value of conditioned reaction; Soda acid required in the electrolytic process is by soda acid storage device 1 deposit.Start power switch 14 according to the pollutent characteristic then, be adjusted to required strength of current by regulating strength of current adjusting knob 16, strength of current numerical value is read by strength of current display instrument 13.Open stirring and adjusting knob 15, control stirring intensity by the velocity of rotation of rotor 5, it is stirred, stirring intensity numerical value is read by stirring intensity display instrument 12.Be provided with plate 7 and cathode plate 6 in the reaction tank, open gas meter 10 and make it pass through aeration head 9 at cathode plate 6 place's aerations.Along with the carrying out of reaction, the pH value in the middle of the solution will change, and the potential of hydrogen in the solution is measured by pH probe 4 at this moment, and reads the pH value by pH display instrument 11.Water after the processing is discharged by water outlet 18.Pool bottom sludge and throw out are discharged by mud discharging mouth 19.
Integral reactor can be with the function (a: add hydrogen peroxide of four kinds of forms of common electrical-Fenton (Fenton) method; B: add Fe
2+C: add hydrogen peroxide and Fe simultaneously
2+D: needn't add hydrogen peroxide and Fe
2+) roll into one, if change the form of electricity-Fenton (Fenton) method, only need can realize multiple function by change electrode pad and control aeration switch.
Claims (7)
1. integral reactor is characterized in that this reactor comprises main reaction pond, base, pH regulator equipment and pH means of detection; Described base is provided with voltage stabilized source, whipping device, indicating instrument, aerator, and pH regulator equipment places side top, main reaction pond, and the pH means of detection places inside, main reaction pond.
2. integral reactor according to claim 1 is characterized in that: described whipping device is the rotor (5) that is located at bottom, main reaction pond.
3. integral reactor according to claim 1 is characterized in that: indicating instrument comprises pH value display instrument (11), stirring intensity display instrument (12) and strength of current display instrument (13).
4. integral reactor according to claim 1 is characterized in that: aerator comprises gas meter (10) and aeration head (9).
5. integral reactor according to claim 1 is characterized in that: described pH regulator equipment is the soda acid storage device (1) that is provided with acid-adding port (2), adds alkali mouth (3).
6. integral reactor according to claim 1 is characterized in that: described pH means of detection is a pH probe (4).
7. integral reactor according to claim 1 is characterized in that: be provided with cathode plate (6) and plate (7) in the main reaction pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620091451 CN2934215Y (en) | 2006-06-09 | 2006-06-09 | Integral reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620091451 CN2934215Y (en) | 2006-06-09 | 2006-06-09 | Integral reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2934215Y true CN2934215Y (en) | 2007-08-15 |
Family
ID=38350903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620091451 Expired - Fee Related CN2934215Y (en) | 2006-06-09 | 2006-06-09 | Integral reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2934215Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101844822A (en) * | 2010-05-11 | 2010-09-29 | 沈阳建筑大学 | Three-dimensional electrode/ electro-Fenton reactor |
-
2006
- 2006-06-09 CN CN 200620091451 patent/CN2934215Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101844822A (en) * | 2010-05-11 | 2010-09-29 | 沈阳建筑大学 | Three-dimensional electrode/ electro-Fenton reactor |
| CN101844822B (en) * | 2010-05-11 | 2012-09-26 | 沈阳建筑大学 | Three-dimensional electrode/ electro-Fenton reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |