CN203866078U - Cylindrical micro electrolytic tower - Google Patents
Cylindrical micro electrolytic tower Download PDFInfo
- Publication number
- CN203866078U CN203866078U CN201420139913.7U CN201420139913U CN203866078U CN 203866078 U CN203866078 U CN 203866078U CN 201420139913 U CN201420139913 U CN 201420139913U CN 203866078 U CN203866078 U CN 203866078U
- Authority
- CN
- China
- Prior art keywords
- tower
- tower body
- water
- outlet section
- water outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 238000005868 electrolysis reaction Methods 0.000 claims description 19
- 239000002351 wastewater Substances 0.000 abstract description 19
- 239000000945 filler Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 5
- 238000004065 wastewater treatment Methods 0.000 abstract description 3
- 230000003139 buffering effect Effects 0.000 abstract description 2
- 230000002035 prolonged effect Effects 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 15
- 229910052742 iron Inorganic materials 0.000 description 8
- 239000003610 charcoal Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 4
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Abstract
The utility model discloses a cylindrical micro electrolytic tower, which comprises a tower body and a water inlet pipe which enters the tower body from the bottom of the tower body; the water inlet pipe comprises a water inlet section positioned at the outer part of the tower body and a water outlet section positioned in the inner part of the tower body; the water outlet section is vertically arranged; an inverted cone-shaped buffer rack is arranged on the periphery of the water outlet section; a cone-shaped buffer cover is arranged above the water outlet section. According to the cylindrical micro electrolytic tower, the inverted cone-shaped buffer rack is arranged on the water outlet section of the water inlet pipe, and the cone-shaped buffer cover is arranged above the water outlet section, so that waste water firstly enters the space between the water outlet section and the buffer rack after flowing out of the water outlet section, and then overflows from the buffer rack; and besides, the buffer cover effectively prevents the waste water from directly rushing into a filler area, so that the water inflowing and buffering effects are obvious, the contact time of the waste water and filler is prolonged, and the wastewater treatment effect is improved.
Description
Technical field
The utility model relates to a kind of micro-electrolysis tower, is specifically related to a kind of cylinder electrolysis tower that declines.
Background technology
Micro-electrolysis tower is equipment general in wastewater treatment, and waste water, by reacting with iron charcoal, is utilized to the reductibility of iron, the electrochemistry of iron charcoal is opened the phenyl ring in difficult biochemical organism; And utilize the flocculation adsorption of iron ion to purify liquid waste.In this microelectrolysis processing process, effective duration of contact of the length of waste water and iron-carbon filling material has important impact for water treatment effect, and be the research direction of this area the effective duration of contact that how to extend waste water and iron-carbon filling material.
Utility model content
Technical problem to be solved in the utility model is, a kind of cylinder electrolysis tower that declines is provided, this electrolysis tower by water intake velocity and in tower body the residence time control, extend effective duration of contact of waste water and iron-carbon filling material.
For solving the problems of the technologies described above, the cylinder of the present utility model electrolysis tower that declines, comprise tower body and enter the water inlet pipe in tower body from tower body bottom, described water inlet pipe comprises the inlet segment that is positioned at tower body outside and the water exit end that is positioned at tower body inside, described water exit end vertically arranges, and the periphery at this water exit end is provided with an obconic buffer rack, is provided with conical impact-absorbing shell above this water exit end.
Further, the buffer rack top sides of described back taper along position lower than the tip position of water exit end.
Further, the conical bottom radius r of described buffer rack is less than the conical bottom radius R of impact-absorbing shell, and buffer rack is enclosed in impact-absorbing shell.
Further, described impact-absorbing shell is fixed in tower body by support bar.
Further, the cone angle alpha of described buffer rack is 90-120 °; The cone angle beta of described impact-absorbing shell is 120-135 °, guarantees that water inlet evenly.
Further, on water inlet pipe, be also communicated with recoil tube, for the flushing of micro-electrolysis tower.
Further, the ratio of the height H of described tower body and diameter D, between 4:1 to 6:1, can make iron charcoal be and seethe shape under setting flooding quantity condition.
The utility model arranges obconic buffer rack by the water exit end at water inlet pipe, and conical impact-absorbing shell is set above water exit end, thereby make waste water from water exit end is gone out, first enter the space between water exit end and buffer rack, then overflow from this buffer rack; Impact-absorbing shell has effectively stopped that waste water is directly toward packing area punching, so its water inlet buffering effect is obvious, thereby has greatly extended the duration of contact of waste water and filler.By setting height and the diameter of the tower body of seasoning iron charcoal and sewage, compare between 4:1 to 6:1, setting under suitable flooding quantity condition like this, can make iron charcoal be to seethe shape can not run off from upper head piece again, make waste water and filler all the time in effective contact condition, effectively improved the water treatment effect of micro-electrolysis tower.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model.
Number in the figure: 1-tower body; 2-tower seat; 3-water inlet pipe; 31-inlet segment; 32-water exit end; 4-recoil tube; 5-buffer rack; 6-impact-absorbing shell; 7-support bar; 8-back up pad.
Embodiment
Embodiment 1 of the present utility model:
As Fig. 1, tower body 1 is fixing by tower seat 2, water inlet pipe 3 enters from tower body 1 bottom in tower body 1 and (from tower seat 2, through tower body 1 bottom, stretches in tower body 1 as shown in Figure 1), described water inlet pipe 3 comprises that the inlet segment 31(that is positioned at tower body 1 outside is positioned at tower seat 2 as shown in Figure 1, this inlet segment 31 is communicated with the outside waste water producing) and be positioned at the water exit end 32 of tower body 1 inside, described water exit end 32 vertically arranges.Waste water, from water exit end 32 ejections, through being arranged on after the interior back up pad with holes 8 of tower body 1, contacts with the filler that is positioned at back up pad 8 tops, thereby micro-electrolysis reaction occurs, and waste water is purified.If waste water directly sprays from water exit end 32, waste water is easy to moment and rushes at filler, and Rapid Flow discharges from micro-electrolysis tower after filler, has a strong impact on water treatment effect.Accordingly, the utility model is provided with an obconic buffer rack 5 in the periphery of this water exit end 32, and above this water exit end 32, is provided with conical impact-absorbing shell 6, and this impact-absorbing shell 6 is fixed in tower body 1 by support bar 7.
Wherein, buffer rack 5 top sides of back taper along position lower than the tip position of water exit end 32; The conical bottom radius r of buffer rack 5 is less than the conical bottom radius R of impact-absorbing shell 6.
The cone angle alpha of described buffer rack 5 is 90-120 °; The cone angle beta of described impact-absorbing shell is 120-135 °, sets this angular range, can guarantee that water inlet evenly.
Waste water is entered by inlet segment 31, from water exit end 32 ejections, enter in obconic buffer rack 5, then from obconic buffer rack 5 edges, overflow, from the space between buffer rack 5 and impact-absorbing shell 6, flow into tower body 1 bottom, from the space between impact-absorbing shell 6 and tower body 1, be slowly upward through back up pad with holes 8 again, and contact with the iron-carbon filling material in back up pad 8.Good shock absorption has been played in 6 pairs of water inlets of buffer rack 5 and impact-absorbing shell, has controlled discharge, has prevented from directly spraying to filler from water exit end 32 waste water out, causes short phenomenon generation duration of contact.
Simultaneously, the ratio of the height H of tower body 1 and diameter D is between 4:1 to 6:1, under setting flooding quantity condition, can make iron charcoal be and seethe shape, and can not run off from upper head piece again, so just can make waste water and filler all the time in effective contact condition, effectively improve the water treatment effect of micro-electrolysis tower.
According to wastewater treatment demand, on water inlet pipe 3, be also communicated with recoil tube 4, this recoil tube 4 is connected on the inlet segment 31 of water inlet pipe 3, and its discharge is greater than the discharge of water inlet pipe 3, thereby makes when equipment is interior, and bonding occurs to rinse.
Above-mentioned embodiment is exemplary, is to be the restriction to the utility model protection domain in order better to make those skilled in the art can understand the utility model, can not to be interpreted as; So long as any being equal to of having done according to spirit that the utility model discloses changes or modify, all fall into the scope of the utility model protection.
Claims (7)
1. the cylinder electrolysis tower that declines, comprise tower body (1) and enter the water inlet pipe (3) in tower body (1) from tower body (1) bottom, described water inlet pipe (3) comprises the water exit end (32) that is positioned at the outside inlet segment (31) of tower body (1) and is positioned at tower body (1) inside, it is characterized in that: described water exit end (32) vertically arranges, and the periphery at this water exit end (32) is provided with an obconic buffer rack (5), in this water exit end (32) top, be provided with conical impact-absorbing shell (6).
2. the cylinder according to claim 1 electrolysis tower that declines, is characterized in that: the buffer rack of described back taper (5) top sides along position lower than the tip position of water exit end (32).
3. the cylinder according to claim 1 electrolysis tower that declines, is characterized in that: the conical bottom radius r of described buffer rack (5) is less than the conical bottom radius R of impact-absorbing shell (6).
4. according to the electrolysis tower that declines of the cylinder described in claim 1 or 3, it is characterized in that: described impact-absorbing shell (6) is fixed in tower body (1) by support bar (7).
5. according to the electrolysis tower that declines of the cylinder described in claim 1 or 3, it is characterized in that: the cone angle alpha of described buffer rack (5) is 90-120 °; The cone angle beta of described impact-absorbing shell (6) is 120-135 °.
6. the cylinder according to claim 1 electrolysis tower that declines, is characterized in that: on water inlet pipe (3), be also communicated with recoil tube (4).
7. the cylinder according to claim 1 electrolysis tower that declines, is characterized in that: the height H of described tower body (1) and the ratio of diameter D are between 4:1 to 6:1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420139913.7U CN203866078U (en) | 2014-03-26 | 2014-03-26 | Cylindrical micro electrolytic tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420139913.7U CN203866078U (en) | 2014-03-26 | 2014-03-26 | Cylindrical micro electrolytic tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203866078U true CN203866078U (en) | 2014-10-08 |
Family
ID=51647057
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420139913.7U Expired - Lifetime CN203866078U (en) | 2014-03-26 | 2014-03-26 | Cylindrical micro electrolytic tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203866078U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697985A (en) * | 2017-11-27 | 2018-02-16 | 山东赛恩环保设备有限公司 | A kind of circulating iron carbon reduction reaction device |
| CN109364832A (en) * | 2018-10-30 | 2019-02-22 | 江苏中圣压力容器装备制造有限公司 | A kind of super isothermal reactor current-equalizing system of large size |
-
2014
- 2014-03-26 CN CN201420139913.7U patent/CN203866078U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107697985A (en) * | 2017-11-27 | 2018-02-16 | 山东赛恩环保设备有限公司 | A kind of circulating iron carbon reduction reaction device |
| CN109364832A (en) * | 2018-10-30 | 2019-02-22 | 江苏中圣压力容器装备制造有限公司 | A kind of super isothermal reactor current-equalizing system of large size |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 324202 Changshan County, Zhejiang Province Ecological Industrial Park, Sheng Sheng Road Patentee after: ZHEJIANG EVER JOINT NEW MATERIAL TECHNOLOGY CO.,LTD. Address before: 324202 Changshan County, Zhejiang Province Ecological Industrial Park, Sheng Sheng Road Patentee before: ZHEJIANG EVER JIONT CHEMICAL CO.,LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141008 |