CN204079553U - A kind of iron-carbon micro-electrolysis reaction unit - Google Patents
A kind of iron-carbon micro-electrolysis reaction unit Download PDFInfo
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- CN204079553U CN204079553U CN201420504521.6U CN201420504521U CN204079553U CN 204079553 U CN204079553 U CN 204079553U CN 201420504521 U CN201420504521 U CN 201420504521U CN 204079553 U CN204079553 U CN 204079553U
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Abstract
The utility model discloses a kind of iron-carbon micro-electrolysis reaction unit, comprise reaction vessel, it is characterized in that: be provided with baffle plate isolation in described reaction vessel and be set to the first reaction zone and second reaction zone, described reaction vessel in the horizontal direction interval arranges two or more bridging plates, bridging plate is provided with bridging pipe, a water inlet pipe is provided with in described reaction vessel, a rising pipe and plural backwash tube, described reaction container bottom is provided with deslagging bucket and scum pipe, its technique effect be the simple laid down cost of this iron-carbon micro-electrolysis reaction unit structure low while can solve iron dirt preferably, the problem of water-flowing path blocking, ensure that the abundant contact reacts of waste water and iron carbon filler, and effectively dirty compound matter punching is fallen, discharge.And the design of bridging cylinder is when meeting full iron carbon filler, artificial maintenance is easy, saves the expense of lifting rig, convenient maintenance and replacement.
Description
Technical field
The utility model relates to a kind of iron-carbon micro-electrolysis reaction unit.
Background technology
Along with the development of whole water treatment field, iron-carbon micro-electrolysis technology is very active in Industrial Wastewater Treatment, it shows higher chroma removal rate to this type of waste water, and its as biochemical reaction pre-treatment, not only improve the biodegradability of waste water, also can remove the material of part to microbial kill.Iron carbon filler is varied in the market, form can be oblateness, spherical, porous column shape etc., but each producer mainly focuses on the development & production of filler, and lack can a kind of high-level efficiency and be easy to the reaction unit of repair and maintenance, to solve after iron carbon filler adds, due to the inconvenience of running maintenance, and the removal effect caused situation worse and worse; And present most of reaction unit is all constructed by steel concrete, causes fabrication cost high, maintenance runs difficult problem.
Summary of the invention
The purpose of this utility model provides a kind of structure simple economy, easy examine and replace, high efficiency iron-carbon micro-electrolysis reaction unit to solve above-mentioned the deficiencies in the prior art.
To achieve these goals, a kind of iron-carbon micro-electrolysis reaction unit designed by the utility model, comprise reaction vessel, be provided with baffle plate isolation in described reaction vessel and be set to the first reaction zone and second reaction zone, prevent short stream, under the condition of aeration, waste water fully contacts with iron carbon filler in reaction zone, reacts completely.Described reaction vessel in the horizontal direction interval arranges two or more bridging plates, bridging plate is provided with bridging pipe, a water inlet pipe, a rising pipe and plural backwash tube is provided with in the described reaction vessel of institute, described water inlet pipe horizontal bore in reactor, make more to disperse into water, fully contact with iron carbon filler.Described counter-flushing pipeline, both can connect middle water, also can connect air, do flushing pipeline during back flushing, also doublely can do aerating pipelines and carry out waste water mixing reaction during reaction.Described reaction container bottom is provided with deslagging bucket and scum pipe.
One section of described bridging pipe is connected with narrow meshed plate, the bridging pipe the other end is provided with the flange plate being greater than pipe diameter, described flange plate connects to hang on bridging plate with bridging plate, and be unlikely to mobile, come off, described bridging pipe sidewall has also been evenly arranged aperture, soft mesh bag is provided with inside bridging pipe, iron carbon filler is filled with in described soft mesh bag, both ensure that iron carbon filler not easily dropped out in cylinder, the abundant contact reacts of waste water and iron carbon filler can be ensure that again, mesh bag is arranged manually can mention maintenance, save the expense of lifting rig, described bridging cylinder liner mesh bag can according to the form of iron carbon filler, size makes.
Described backwash tube is fixed along reaction vessel inwall by clip, and ring center internally level is provided with perforate.Described reaction vessel is provided with boring aeration pipe, and boring aeration pipe can be arranged in reaction vessel in H type.Adopt Flange joint in described boring aeration pipe main line and reaction vessel, boring aeration pipe for subsequent use can be carried out, shorten the repair time.
Described bridging plate is arranged respectively two inspection manholes, described inspection manhole diagonal angle is arranged at baffle plate both sides, the inspection manhole arranged crosswise between each layer and each layer.
A kind of iron-carbon micro-electrolysis reaction unit that the utility model obtains, its technique effect be the simple laid down cost of this iron-carbon micro-electrolysis reaction unit structure low while can solve iron dirt preferably, the problem of water-flowing path blocking, ensure that the abundant contact reacts of waste water and iron carbon filler, and effectively dirty compound matter punching is fallen, discharge.And the design of bridging cylinder is when meeting full iron carbon filler, artificial maintenance is easy, saves the expense of lifting rig, convenient maintenance and replacement.
Accompanying drawing explanation
Fig. 1 is the iron carbon reaction unit structural representation of embodiment 1;
Fig. 2 is the water inlet distributor perforate schematic diagram of embodiment 1;
Fig. 3 is that the counter-flushing pipeline of embodiment 1 arranges schematic diagram;
Fig. 4 is the bridging plate structure schematic diagram of embodiment 1;
Fig. 5 is the bridging cylinder schematic diagram of embodiment 1;
Fig. 6 is the boring aeration pipeline schematic diagram of embodiment 1.
In figure: reaction vessel 1, baffle plate 2, first reaction zone 3, second reaction zone 4, bridging plate 5, bridging pipe 6, flange plate 6a, water inlet pipe 7, rising pipe 8, backwash tube 9, deslagging bucket 10, scum pipe 11, boring aeration pipe 12, inspection manhole 13.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Embodiment 1:
As shown in Figure 1, a kind of iron-carbon micro-electrolysis reaction unit that the utility model provides, comprise reaction vessel 1, be provided with baffle plate 2 isolation in described reaction vessel 1 and be set to the first reaction zone 3 and second reaction zone 4, prevent short stream, under the condition of aeration, waste water fully contacts with iron carbon filler in reaction zone, reacts completely.Described reaction vessel 1 in the horizontal direction interval arranges the bridging plate 5 of three, bridging plate 5 is provided with bridging pipe 6, as shown in Figures 2 and 3, be provided with the backwash tube 9 of a water inlet pipe 7, rising pipe 8 and two in described reaction vessel 1, bottom described reaction vessel 1, be provided with deslagging bucket 10 and scum pipe 11.Described water inlet pipe horizontal bore in reactor, makes more to disperse into water, fully contacts with iron carbon filler.Do flushing pipeline during back flushing, also doublely can do aerating pipelines during reaction and carry out waste water mixing reaction.
As shown in Figure 4 and Figure 5, one section of described bridging pipe 6 is connected with narrow meshed plate, and bridging pipe 6 the other end is provided with the flange plate 6a being greater than pipe diameter, and described flange plate 6a connects with bridging plate 5, to hang on bridging plate, and is unlikely to mobile, comes off.Described bridging pipe 6 sidewall has also been evenly arranged aperture, is provided with soft mesh bag inside bridging pipe, is filled with iron carbon filler in described soft mesh bag, both ensure that iron carbon filler not easily drops out in cylinder, can ensure that again the abundant contact reacts of waste water and iron carbon filler.
Described backwash tube 9 is fixed along reaction vessel 1 inwall by clip, and ring center internally level is provided with perforate.Described reaction vessel 1 is provided with boring aeration pipe 12, and boring aeration pipe 12 can be arranged in reaction vessel in H type.As shown in Figure 6, adopt Flange joint in described boring aeration pipe 12 main line and reaction vessel, boring aeration pipe 12 for subsequent use can be carried out, shorten the repair time.
Described bridging plate 5 is arranged respectively two inspection manholes 13, described inspection manhole 13 diagonal angle is arranged at baffle plate 2 both sides, inspection manhole 13 arranged crosswise between each layer and each layer.
Embodiment 2:
The structure of a kind of iron-carbon micro-electrolysis reaction unit that the present embodiment 2 provides is substantially the same manner as Example 1, as shown in Figure 1, comprise reaction vessel 1, be provided with baffle plate 2 isolation in described reaction vessel 1 and be set to the first reaction zone 3 and second reaction zone 4, prevent short stream, under the condition of aeration, waste water fully contacts with iron carbon filler in reaction zone, reacts completely.Described reaction vessel 1 in the horizontal direction interval arranges the bridging plate 5 of three, bridging plate 5 is provided with bridging pipe 6, be provided with the backwash tube 9 of a water inlet pipe 7, rising pipe 8 and two in described reaction vessel 1, bottom described reaction vessel 1, be provided with deslagging bucket 10 and scum pipe 11.Described water inlet pipe horizontal bore in reactor, makes more to disperse into water, fully contacts with iron carbon filler.Do flushing pipeline during back flushing, also doublely can do aerating pipelines during reaction and carry out waste water mixing reaction.
But the iron-carbon micro-electrolysis carried out to make waste water reaction is more efficient, as shown in Figure 4 and Figure 5, reaction vessel 1 inside divides three layers to arrange iron carbon filler substantially.Every layer of filler forms by the bridging pipe of certain diameter, and as shown in Figure 4 and Figure 5, one end is by the plate shutoff with aperture (φ=3 ~ 5mm), and the flange plate slightly larger than pipeline diameter is made in one end in addition, to hang on bridging plate, and is unlikely to mobile, comes off; Bridging pipe sidewall is also evenly arranged the aperture (φ=6 ~ 10mm) of some amount; The soft mesh bag of bridging pipe liner (φ=2 ~ 3mm); Place iron carbon filler in mesh bag, bridging cylinder and the readily removable setting removed of bridging plate, can solve iron dirt preferably, and the problem of water-flowing path blocking, meanwhile, this set allows manually to mention maintenance, saves the expense of lifting rig, convenient maintenance and replacement.
One section of described bridging pipe 6 is connected with narrow meshed plate, and bridging pipe 6 the other end is provided with the flange plate 6a being greater than pipe diameter, and described flange plate 6a connects with bridging plate 5, to hang on bridging plate, and is unlikely to mobile, comes off.Described bridging pipe 6 sidewall has also been evenly arranged aperture, is provided with soft mesh bag inside bridging pipe, is filled with iron carbon filler in described soft mesh bag, both ensure that iron carbon filler not easily drops out in cylinder, can ensure that again the abundant contact reacts of waste water and iron carbon filler.
Described backwash tube 9 is fixed along reaction vessel 1 inwall by clip, and ring center internally level is provided with perforate.Described reaction vessel 1 is provided with boring aeration pipe 12, and boring aeration pipe 12 is arranged in reaction vessel in H type.Adopt Flange joint in described boring aeration pipe 12 main line and reaction vessel, boring aeration pipe 12 for subsequent use can be carried out, shorten the repair time.
Described bridging plate 5 is arranged respectively two inspection manholes 13, described inspection manhole 13 diagonal angle is arranged at baffle plate 2 both sides, inspection manhole 13 arranged crosswise between each layer and each layer.
The material of described reaction vessel 1 is glass reinforced plastic, and glass steel reaction unit structure is simple, and floor space is little, and can solve steel concrete structure iron carbon reaction fabrication cost preferably high, maintenance runs difficult problem.
Claims (6)
1. an iron-carbon micro-electrolysis reaction unit, comprise reaction vessel (1), it is characterized in that: be provided with baffle plate (2) isolation in described reaction vessel (1) and be set to the first reaction zone (3) and second reaction zone (4), described reaction vessel (1) in the horizontal direction interval arranges two or more bridging plates (5), bridging plate (5) is provided with bridging pipe (6), a water inlet pipe (7) is provided with in described reaction vessel (1), a rising pipe (8) and plural backwash tube (9), described reaction vessel (1) bottom is provided with deslagging bucket (10) and scum pipe (11).
2. a kind of iron-carbon micro-electrolysis reaction unit according to claim 1, it is characterized in that: one section of described bridging pipe (6) is connected with narrow meshed plate, bridging pipe (6) the other end is provided with the flange plate (6a) being greater than pipe diameter, and described flange plate (6a) connects with bridging plate (5); Described bridging pipe (6) sidewall has also been evenly arranged aperture, is provided with soft mesh bag, is filled with iron carbon filler in described soft mesh bag inside bridging pipe.
3. a kind of iron-carbon micro-electrolysis reaction unit according to claim 1 and 2, is characterized in that: described backwash tube (9) is fixed along reaction vessel (1) inwall by clip, and ring center internally level is provided with perforate.
4. a kind of iron-carbon micro-electrolysis reaction unit according to claim 1 and 2, is characterized in that: described reaction vessel (1) is provided with boring aeration pipe (12), adopts Flange joint in described boring aeration pipe (12) main line and reaction vessel (1).
5. a kind of iron-carbon micro-electrolysis reaction unit according to claim 1 and 2, it is characterized in that: described bridging plate (5) is arranged respectively two inspection manholes (13), described inspection manhole (13) diagonal angle is arranged at baffle plate (2) both sides, inspection manhole (13) arranged crosswise between each layer and each layer.
6. a kind of iron-carbon micro-electrolysis reaction unit according to claim 1 and 2, is characterized in that: the material of described reaction vessel (1) is glass reinforced plastic.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420504521.6U CN204079553U (en) | 2014-09-03 | 2014-09-03 | A kind of iron-carbon micro-electrolysis reaction unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420504521.6U CN204079553U (en) | 2014-09-03 | 2014-09-03 | A kind of iron-carbon micro-electrolysis reaction unit |
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|---|---|
| CN204079553U true CN204079553U (en) | 2015-01-07 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420504521.6U Expired - Fee Related CN204079553U (en) | 2014-09-03 | 2014-09-03 | A kind of iron-carbon micro-electrolysis reaction unit |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106554057A (en) * | 2016-11-25 | 2017-04-05 | 江苏鼎弘环境科技有限公司 | A kind of micro-electrolysis reactor of sewage containing tar |
-
2014
- 2014-09-03 CN CN201420504521.6U patent/CN204079553U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106554057A (en) * | 2016-11-25 | 2017-04-05 | 江苏鼎弘环境科技有限公司 | A kind of micro-electrolysis reactor of sewage containing tar |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20160903 |