CN102701392A - Fenton fluidized bed with monitoring device - Google Patents
Fenton fluidized bed with monitoring device Download PDFInfo
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- CN102701392A CN102701392A CN2012101641649A CN201210164164A CN102701392A CN 102701392 A CN102701392 A CN 102701392A CN 2012101641649 A CN2012101641649 A CN 2012101641649A CN 201210164164 A CN201210164164 A CN 201210164164A CN 102701392 A CN102701392 A CN 102701392A
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- tower body
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- inlet channel
- monitoring device
- fenton fluidized
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Abstract
The invention discloses a Fenton fluidized bed with a monitoring device. The Fenton fluidized bed comprises a tower body, a water inlet channel, a water outlet channel, a water inlet pipeline, a water circulating pump and a medicine feeding pipeline, wherein the water inlet channel and the water outlet channel are respectively arranged at the two sides of the upper end of the tower body; the water inlet channel and the water outlet channel are communicated with an inner cavity of the tower body; the water inlet channel is connected at the bottom of the tower body through the water inlet pipeline; the water circulating pump is arranged on the water inlet pipeline; the medicine feeding pipeline is connected on the water inlet pipeline; and the upper part of the inner cavity of the tower body is provided with a monitoring device used for monitoring water processing quality. With the adoption of the Fenton fluidized bed with the monitoring device, compared with the existing product, the monitoring device is arranged at the upper end inside the tower body; after the sewage and medicine are mixed, the processing quality of the sewage can be effectively monitored; and the Fenton fluidized bed with the monitoring device is simple in structure, is practical and can be used for realizing the purpose of the Fenton fluidized bed.
Description
Technical field
The present invention relates to water treatment field, is a kind of Fenton fluidized-bed with monitoring device specifically.
Background technology
Fluidized-bed is a kind of visual plant of disposing of sewage, and the principle of original biological treatment of sewage is to let airborne oxygen fully contact with sewage, makes airborne oxygen fully be dissolved in sewage.Under some special situation; After airborne oxygen and sewage fully dissolve, still can not effectively handle, just need to add an amount of medicament sewage; Medicament is mixed with sewage, yet existing fluidized-bed can not be done effective monitoring to quality of sewage disposal.
Therefore, need a kind of Fenton fluidized-bed especially, to solve the problem that exists in the prior art with monitoring device.
Summary of the invention
The objective of the invention is in order to solve in the prior art after WWT, the defective that can not handle the sewage quality provides a kind of Fenton fluidized-bed with monitoring device to solve the problems referred to above.
To achieve these goals, technical scheme of the present invention is following:
A kind of Fenton fluidized-bed with monitoring device; Comprise tower body, inlet flume, effluent trough, inlet channel, water circulating pump and drug feeding pipeline; It is characterized in that said inlet flume and effluent trough are arranged at the both sides of tower body upper end respectively, and inlet flume and effluent trough are communicated with the inner chamber of tower body; Said inlet flume is connected the bottom of tower body through inlet channel; Said water circulating pump is arranged on the inlet channel, and said drug feeding pipeline is connected on the inlet channel, and the inner chamber top of said tower body is provided with the monitoring device that is used to monitor the water treatment quality.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device; It is characterized in that said inlet channel is divided into two-way, comprise first inlet channel and second inlet channel; The quantity of water circulating pump and drug feeding pipeline also is two; Two drug feeding pipeline are respectively ferrous sulfate drug feeding pipeline and ydrogen peroxide 50 drug feeding pipeline, and said two water circulating pumps are arranged at respectively on first inlet channel and second inlet channel, and said two drug feeding pipeline connect first inlet channel and second inlet channel respectively.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device is characterized in that the bottom of said tower body inner chamber is provided with water distribution pipe, and said water distribution pipe is provided with water distributing pore, and the two ends of said water distribution pipe connect first inlet channel and second inlet channel.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device is characterized in that, is provided with the iron sand that is used for the boosting reaction in the inner chamber of said tower body.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device is characterized in that, is communicated with through water-in between the inner chamber of said tower body and the inlet flume, is communicated with through water outlet between the inner chamber of said tower body and the effluent trough, and the position of said water-in is lower than the water outlet position.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device is characterized in that said water-in and water outlet are provided with the filter cap.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device; It is characterized in that; Also be provided with in the cavity of said tower body and be used to prevent that iron sand is with liquid level separator that rises and the support bar that is used to support separator; Said support bar one end connects separator, and the support bar the other end is connected on the inwall of inner chamber of tower body.
Above-mentioned a kind of Fenton fluidized-bed with monitoring device is characterized in that said separator and support bar are integral structure.
A kind of Fenton fluidized-bed of the present invention with monitoring device; Compare with currently available products, monitoring device is set, make the present invention after sewage and medicament combination treatment in the tower body inner upper end; Can effectively monitor the processing quality of sewage; Simple in structure, very practical, realize the object of the invention.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Embodiment
For making constitutional features of the present invention and the effect reached there are further understanding and understanding, cooperate detailed explanation, explain as follows in order to preferred embodiment and accompanying drawing:
Referring to Fig. 1; A kind of Fenton fluidized-bed with monitoring device; Comprise tower body 300, inlet flume 100, effluent trough 200, inlet channel 400, water circulating pump 500 and drug feeding pipeline 600, inlet flume 100 and effluent trough 200 are arranged at the both sides of tower body 300 upper ends respectively, and inlet flume 100 is communicated with the inner chamber of tower body 300 with effluent trough 200; Inlet flume 100 is connected the bottom of tower body 300 through inlet channel 400; Water circulating pump 500 is arranged on the inlet channel 400, and drug feeding pipeline 600 is connected on the inlet channel 400, and the inner chamber top of tower body 300 is provided with the monitoring device 700 that is used to monitor the water treatment quality.In work; Sewage flows into inlet channel 400 from inlet flume 100, water circulating pump 500 is used for extracting the drainage flow of inlet channel 500, adds medicine in 600 pairs of sewer lines of drug feeding pipeline then; Sewage and medicine flow into together in the tower body 300 and in the inner chamber of tower body 300 and react; Thereby purify waste water, final purification water later flows out from effluent trough 200, and the effect of monitoring device 700 is in the process that sewage is purifying; Monitoring device can be simultaneously be monitored the water quality after purifying, and adjustment technology parameter at any time.
The bottom of tower body 300 inner chambers is provided with water distribution pipe 810; Water distribution pipe 810 is provided with water distributing pore 820; The two ends of water distribution pipe 810 connect first inlet channel 410 and second inlet channel 420; The sewage that has added in first inlet channel 410 of ferrous sulfate flows in the water distribution pipe 810 from an end of water distribution pipe 810, from water distributing pore 820, is sprayed onto in the inner chamber of tower body 300 then; The sewage that has added in second inlet channel 420 of ferrous sulfate flows in the water distribution pipe 810 from an end of water distribution pipe 810, from water distributing pore 820, sprays out then.The sewage that is added with ferrous sulfate reacts with iron sand 830 in the inner chamber of tower body 300 with the sewage that is added with ydrogen peroxide 50, thereby sewage is purified.
Be provided with the iron sand 830 that is used for the boosting reaction in the inner chamber of tower body 300; Because entering into the sewage of the inner chamber purification reaction of tower body 300 gets more and more; Liquid level in the inner chamber can rise accordingly, and in medicament and the sewage reflection process, iron sand 830 is used to make better reacting with sewage of medicament.
Be communicated with through water-in 110 between the inner chamber of tower body 300 and the inlet flume 100; Be communicated with through water outlet 210 between the inner chamber of tower body 300 and the effluent trough 200; Purifying a water part later flows back in the inlet flume 100 through water-in 110; Form a backflow and purify once more, the water of another part then directly flows in the effluent trough 200 through water outlet 210.Water-in 110 is provided with filter cap 120, and water outlet 210 is provided with filter cap 220, and the effect of filter cap 120 and filter cap 220 is the suspended matter on sewage surface has also been played filtering effect.
The position of water-in 110 is lower than the position of water outlet 210; In real work, after the liquid level in the inner chamber of tower body 300 rises, at first can arrive the position of water-in 110; The water of a part can flow back in the inlet flume 100 circularly purifying again from water-in 110; And when liquid level continuation rising, liquid level arrives the position of water outlet 210, flow into the effluent trough 200 from water outlet 210 again.
Also be provided with in the cavity of tower body 300 and be used for iron sand with liquid level separator 840 that rises and the support bar 850 that is used to support separator 840; Separator 840 is a turbination; Conical top is provided with opening, and support bar 850 has four, and support bar 850 1 ends connect separator 840; Support bar 850 the other ends are connected on the inwall of inner chamber of tower body 300, and separator 840 is an integral structure with support bar 850.
The present invention compares with currently available products, in the tower body inner upper end monitoring device is set, and makes the present invention after sewage and medicament combination treatment, can effectively monitor the processing quality of sewage, and is simple in structure, very practical.
More than show and described ultimate principle of the present invention, principal character and advantage of the present invention.The technician of the industry should understand; The present invention is not restricted to the described embodiments; What describe in the foregoing description and the specification sheets is principle of the present invention; The present invention also has various changes and modifications under the prerequisite that does not break away from spirit and scope of the invention, and these variations and improvement all fall in the scope of the present invention that requires protection.The protection domain that the present invention requires is defined by appending claims and equivalent thereof.
Claims (8)
1. Fenton fluidized-bed with monitoring device; Comprise tower body, inlet flume, effluent trough, inlet channel, water circulating pump and drug feeding pipeline; It is characterized in that said inlet flume and effluent trough are arranged at the both sides of tower body upper end respectively, and inlet flume and effluent trough are communicated with the inner chamber of tower body; Said inlet flume is connected the bottom of tower body through inlet channel; Said water circulating pump is arranged on the inlet channel, and said drug feeding pipeline is connected on the inlet channel, and the inner chamber top of said tower body is provided with the monitoring device that is used to monitor the water treatment quality.
2. a kind of Fenton fluidized-bed according to claim 1 with monitoring device; It is characterized in that; Said inlet channel is divided into two-way; Comprise first inlet channel and second inlet channel, the quantity of water circulating pump and drug feeding pipeline also is two, and two drug feeding pipeline are respectively ferrous sulfate drug feeding pipeline and ydrogen peroxide 50 drug feeding pipeline; Said two water circulating pumps are arranged at respectively on first inlet channel and second inlet channel, and said two drug feeding pipeline connect first inlet channel and second inlet channel respectively.
3. a kind of Fenton fluidized-bed according to claim 2 with monitoring device; It is characterized in that; The bottom of said tower body inner chamber is provided with water distribution pipe, and said water distribution pipe is provided with water distributing pore, and the two ends of said water distribution pipe connect first inlet channel and second inlet channel.
4. according to any described a kind of Fenton fluidized-bed among the claim 1-3, it is characterized in that, be provided with the iron sand that is used for the boosting reaction in the inner chamber of said tower body with monitoring device.
5. a kind of Fenton fluidized-bed according to claim 4 with monitoring device; It is characterized in that; Be communicated with through water-in between the inner chamber of said tower body and the inlet flume, be communicated with through water outlet between the inner chamber of said tower body and the effluent trough, the position of said water-in is lower than the water outlet position.
6. a kind of Fenton fluidized-bed with monitoring device according to claim 5 is characterized in that said water-in and water outlet are provided with the filter cap.
7. a kind of Fenton fluidized-bed according to claim 6 with monitoring device; It is characterized in that; Also be provided with in the cavity of said tower body and be used to prevent that iron sand is with liquid level separator that rises and the support bar that is used to support separator; Said support bar one end connects separator, and the support bar the other end is connected on the inwall of inner chamber of tower body.
8. a kind of Fenton fluidized-bed with monitoring device according to claim 7 is characterized in that said separator and support bar are integral structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101641649A CN102701392A (en) | 2012-05-24 | 2012-05-24 | Fenton fluidized bed with monitoring device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2012101641649A CN102701392A (en) | 2012-05-24 | 2012-05-24 | Fenton fluidized bed with monitoring device |
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| CN102701392A true CN102701392A (en) | 2012-10-03 |
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| CN2012101641649A Pending CN102701392A (en) | 2012-05-24 | 2012-05-24 | Fenton fluidized bed with monitoring device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
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| US6143182A (en) * | 1998-05-01 | 2000-11-07 | Industrial Technology Research Institute | Process for chemically oxidizing wastewater with reduced sludge production |
| CN101104539A (en) * | 2007-07-31 | 2008-01-16 | 华南理工大学 | Alga-bacterium symbiosis fluid bed treatment system for high concentrated organic wastewater |
| CN101519251A (en) * | 2009-04-09 | 2009-09-02 | 广西大学 | Process for treating bio-refractory waste water by up-flow multi-phase oxidation column |
| CN201376913Y (en) * | 2009-04-09 | 2010-01-06 | 广西博世科环保科技有限公司 | Up-flowing multi-phase waste-water processing oxidation tower |
| CN201665597U (en) * | 2010-04-01 | 2010-12-08 | 上海申兰环保有限公司 | Device for processing the waste water using a micro-electrolysis and Fenton coupling technology |
| CN101993144A (en) * | 2010-12-17 | 2011-03-30 | 江苏江大环境工程有限责任公司 | Catalytic oxidation fluid bed |
| CN102249393A (en) * | 2011-06-08 | 2011-11-23 | 武汉凯迪水务有限公司 | Circulating fluidized bed advanced treatment equipment for industrial wastewater |
| CN202139138U (en) * | 2011-07-20 | 2012-02-08 | 浙江环科环境研究院有限公司 | Improved Fenton fluidized bed waste water treatment device |
| CN202643405U (en) * | 2012-05-24 | 2013-01-02 | 苏州顶裕水务科技有限公司 | Fenton fluidized bed with monitoring device |
-
2012
- 2012-05-24 CN CN2012101641649A patent/CN102701392A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6143182A (en) * | 1998-05-01 | 2000-11-07 | Industrial Technology Research Institute | Process for chemically oxidizing wastewater with reduced sludge production |
| CN101104539A (en) * | 2007-07-31 | 2008-01-16 | 华南理工大学 | Alga-bacterium symbiosis fluid bed treatment system for high concentrated organic wastewater |
| CN101519251A (en) * | 2009-04-09 | 2009-09-02 | 广西大学 | Process for treating bio-refractory waste water by up-flow multi-phase oxidation column |
| CN201376913Y (en) * | 2009-04-09 | 2010-01-06 | 广西博世科环保科技有限公司 | Up-flowing multi-phase waste-water processing oxidation tower |
| CN201665597U (en) * | 2010-04-01 | 2010-12-08 | 上海申兰环保有限公司 | Device for processing the waste water using a micro-electrolysis and Fenton coupling technology |
| CN101993144A (en) * | 2010-12-17 | 2011-03-30 | 江苏江大环境工程有限责任公司 | Catalytic oxidation fluid bed |
| CN102249393A (en) * | 2011-06-08 | 2011-11-23 | 武汉凯迪水务有限公司 | Circulating fluidized bed advanced treatment equipment for industrial wastewater |
| CN202139138U (en) * | 2011-07-20 | 2012-02-08 | 浙江环科环境研究院有限公司 | Improved Fenton fluidized bed waste water treatment device |
| CN202643405U (en) * | 2012-05-24 | 2013-01-02 | 苏州顶裕水务科技有限公司 | Fenton fluidized bed with monitoring device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
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Application publication date: 20121003 |