CN204607826U - A kind of sludge ozone cracks reactor - Google Patents
A kind of sludge ozone cracks reactor Download PDFInfo
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- CN204607826U CN204607826U CN201520195409.3U CN201520195409U CN204607826U CN 204607826 U CN204607826 U CN 204607826U CN 201520195409 U CN201520195409 U CN 201520195409U CN 204607826 U CN204607826 U CN 204607826U
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- mud
- ozone
- oxidizing tower
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- ozonizer
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a kind of sludge ozone and crack reactor, be made up of air compressor, drying installation, ozonizer, mud oxidizing tower, recycle pump, exhaust gas treating tower, strainer and settling tank, it is characterized in that: described air compressor connects drying installation, ozonizer, flow of ozone gauge and ozone import successively; Described strainer is arranged on between mud pipe and mud inlet; Catalytic filler is provided with in described mud oxidizing tower; Described mud oxidizing tower inside is provided with water distribution board; Described mud oxidizing tower upper side is provided with mud inlet.Native system is integrated with ozone oxidation, precipitation process, by ozone oxidation, the microorganism in mud is cracked, accelerate mud organic substance release, the mud cracked is easy to dehydration, water extracter energy consumption reduces, and mud has germicidal action by oxidation simultaneously, has the utilization ratio improving ozone, can recycle tail gas, the advantage that device is compact and floor space is less.
Description
Technical field
The utility model relates to a kind of sludge ozone and cracks reactor.
Background technology
Along with the quantity discharged of sewage is increasing, wastewater treatment rate also improves year by year, and the sludge yield of sewage work also sharply increases, a large amount of excess sludges will discharge in sewage work, the mud of enormous amount needs to do further process, if mud can not get reasonable process, will cause secondary pollution.At present urban sludge treating method is had multiple, generally have landfill, burning and comprehensive utilization, but before recycling, pre-treatment need be carried out to mud, carry out cracking conditioning etc., comprise concentrated, dehydration, dry.In the mud gravity concentration tank of sewage work, mud is by after natural subsidence gravity concentration, remove the free water in mud, mud needs to carry out decrement disposal, containing microorganism in mud, anaerobic digestion time is a very long process, acidication speed is very slow, and therefore mud needs to carry out cracking process, accelerates mud organic substance release.Ozone is universally acknowledged broad-spectrum high efficacy disinfection sanitizer, air or oxygen is adopted to be that the electric discharge of prepared using high-frequency and high-voltage produces ozone, ozone is more than an oxygen molecule active Sauerstoffatom ozone, chemical property is active especially, it is a kind of strong oxidizer, the bacterium in air can be killed rapidly under finite concentration, without any poisonous residual, secondary pollution can not be formed, ozonizer principle of work is by the model split of ozone generation, and ozonizer mainly contains three kinds: high voltage discharge type, uviolizing formula, electrolyzing.In Water Disinfection and sewage treatment area also widespread use, by ozone by killing bacteria in water, by organic matter degradation, existing ozone oxidation adopts the mode in pond, and there is ozone utilization rate not high, tail gas is random discharge, so need a kind of sludge ozone to crack reactor, improve the utilization ratio of ozone, mud is oxidized more thorough, and can recycle tail gas.
Utility model content
The purpose of this utility model is to provide a kind of sludge ozone to crack reactor, native system is integrated with ozone oxidation, precipitation process, by ozone oxidation, the microorganism in mud is cracked, accelerate mud organic substance release, the mud cracked is easy to dehydration, and water extracter energy consumption reduces, mud has germicidal action by oxidation simultaneously, have and improve the utilization ratio of ozone, can recycle tail gas, the advantage that device is compact and floor space is less.
The purpose of this utility model is achieved through the following technical solutions: a kind of sludge ozone cracks reactor, be made up of air compressor, drying installation, ozonizer, mud oxidizing tower, recycle pump, exhaust gas treating tower, strainer and settling tank, it is characterized in that: described air compressor connects drying installation, ozonizer, flow of ozone gauge and ozone import successively; Described strainer is arranged on between mud pipe and mud inlet; Catalytic filler is provided with in described mud oxidizing tower; Described mud oxidizing tower inside is provided with water distribution board; Described mud oxidizing tower upper side is provided with mud inlet.
Be provided with mud discharging mouth bottom described mud oxidizing tower, mud discharging mouth is connected with settling tank by pipeline, and is provided with recycle pump on circulation tube.
The top of described mud oxidizing tower is provided with exhaust port, and exhaust port is connected with exhaust gas treating tower by pipeline.
Utility model works principle: air enters air compressor and compressed, need to lower the temperature in water cooler because temperature raises, then enter in drying installation, compression, dried air are metered into ozonizer, high-voltage corona electric field is manufactured at the high-tension current of certain frequency, make the oxygen molecule generation electrochemical reaction in electric field or around electric field, generate ozone by electrolysis air.In ozone generating unit operational process, temperature raises, and passes into water coolant from entrance of cooling water, and cooling ozone generating unit, makes its working stability, improve the work-ing life of ozone generating unit.Ozone enters mud oxidizing tower from bottom to top from ozone import after the metering of flow of ozone gauge, the water of oxidation is needed to enter mud oxidizing tower from top to bottom from the mud inlet of mud oxidizing tower upper side, uniform liquid is distributed by water distribution board, gas-liquid mass transfer is carried out in catalytic filler, in water, bacterium is killed, organism is degraded, and oxidated solution body is discharged from mud discharging mouth, and tail gas is discharged from the exhaust port at mud oxidizing tower top.In mud oxidizing tower, drop into the strong oxidizers such as ozone, cell content is released, and kill bacterium in mud, thus significantly improve the content of protein in mud, carrying out fast of facilitation of hydrolysis.
In sum, the beneficial effects of the utility model: native system is integrated with ozone oxidation, precipitation process, by ozone oxidation, the microorganism in mud is cracked, accelerate mud organic substance release, the mud cracked is easy to dehydration, and water extracter energy consumption reduces, mud has germicidal action by oxidation simultaneously, have and improve the utilization ratio of ozone, can recycle tail gas, the advantage that device is compact and floor space is less.Catalytic filler is used to accelerate sludge disintegration reaction.
Accompanying drawing explanation
Fig. 1 structural representation of the present utility model.
The title marked in accompanying drawing: 1-air compressor; 2-drying installation; 3-ozonizer; 4-flow of ozone gauge; 5-mud oxidizing tower; 6-water distribution board; 7-exhaust port; 8-catalytic filler; The import of 9-ozone; 10-mud inlet; 11-enter mud pipe; 12-form; 13-access hole; 14-mud discharging mouth; 15-recycle pump; 16-circulation tube; 17-exhaust gas treating tower; 18-strainer; 19-settling tank.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, but embodiment of the present utility model is not limited only to this.
Embodiment: as shown in Figure 1, a kind of sludge ozone cracks reactor, be made up of air compressor (1), drying installation (2), ozonizer (3), mud oxidizing tower (5), recycle pump (15), exhaust gas treating tower (17), strainer (18) and settling tank (19), it is characterized in that: described air compressor (1) connects drying installation (2), ozonizer (3), flow of ozone gauge (4) and ozone import (9) successively; Described strainer (18) is arranged on between mud pipe (11) and mud inlet (10); Catalytic filler (8) is provided with in described mud oxidizing tower (5); Described mud oxidizing tower (5) inside is provided with water distribution board (6); Described mud oxidizing tower (5) upper side is provided with mud inlet (10).
Described mud oxidizing tower (5) bottom is provided with mud discharging mouth (14), and mud discharging mouth (14) is connected with settling tank (19) by pipeline, and is provided with recycle pump (15) on circulation tube (16).
The top of described mud oxidizing tower (5) is provided with exhaust port (7), and exhaust port (7) is connected with exhaust gas treating tower (17) by pipeline.
During utility model works: air enters air compressor (1) and compressed, need to lower the temperature in water cooler because temperature raises, then enter in drying installation (2), compression, dried air are metered into ozonizer (3), high-voltage corona electric field is manufactured at the high-tension current of certain frequency, make the oxygen molecule generation electrochemical reaction in electric field or around electric field, generate ozone by electrolysis air.In ozone generating unit operational process, temperature raises, and passes into water coolant from entrance of cooling water, and cooling ozone generating unit, makes its working stability, improve the work-ing life of ozone generating unit.Ozone enters mud oxidizing tower (5) from bottom to top from ozone import (9) after flow of ozone gauge (4) metering, the water of oxidation is needed to enter mud oxidizing tower (5) from top to bottom from the mud inlet (10) of mud oxidizing tower (5) upper side, uniform liquid is distributed by water distribution board (6), carry out gas-liquid mass transfer catalytic filler (8) is inner, in water, bacterium is killed, organism is degraded, oxidated solution body is discharged from mud discharging mouth (14), and tail gas is discharged from the exhaust port (7) at mud oxidizing tower (5) top.In mud oxidizing tower (5), drop into the strong oxidizers such as ozone, cell content is released, and kills bacterium in mud, thus significantly improve the content of protein in mud, carrying out fast of facilitation of hydrolysis.
As mentioned above, just the utility model can be realized preferably.
Claims (2)
1. a sludge ozone cracks reactor, be made up of air compressor (1), drying installation (2), ozonizer (3), mud oxidizing tower (5), recycle pump (15), exhaust gas treating tower (17), strainer (18) and settling tank (19), it is characterized in that: described air compressor (1) connects drying installation (2), ozonizer (3), flow of ozone gauge (4) and ozone import (9) successively; Described strainer (18) is arranged on between mud pipe (11) and mud inlet (10); Catalytic filler (8) is provided with in described mud oxidizing tower (5); Described mud oxidizing tower (5) inside is provided with water distribution board (6); Described mud oxidizing tower (5) upper side is provided with mud inlet (10); Described mud oxidizing tower (5) bottom is provided with mud discharging mouth (14), and mud discharging mouth (14) is connected with settling tank (19) by pipeline, and is provided with recycle pump (15) on circulation tube (16).
2. a kind of sludge ozone according to claim 1 cracks reactor, it is characterized in that: the top of described mud oxidizing tower (5) is provided with exhaust port (7), and exhaust port (7) is connected with exhaust gas treating tower (17) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520195409.3U CN204607826U (en) | 2015-04-02 | 2015-04-02 | A kind of sludge ozone cracks reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520195409.3U CN204607826U (en) | 2015-04-02 | 2015-04-02 | A kind of sludge ozone cracks reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204607826U true CN204607826U (en) | 2015-09-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201520195409.3U Expired - Fee Related CN204607826U (en) | 2015-04-02 | 2015-04-02 | A kind of sludge ozone cracks reactor |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254154A (en) * | 2015-11-24 | 2016-01-20 | 江苏菲德俐环保科技有限公司 | Biochemical sludge reduction integrated equipment |
| CN107721111A (en) * | 2017-11-10 | 2018-02-23 | 北京宜清源科技有限公司 | A kind of system and method for mud decrement processing |
| CN107879583A (en) * | 2017-12-23 | 2018-04-06 | 北京达源环保科技有限公司 | Sludge pyrohydrolysis and anaerobic digestion integrated treatment process system |
| CN110156255A (en) * | 2019-05-10 | 2019-08-23 | 江苏华晖环保科技有限公司 | A kind of hardly possible biochemical waste water advanced treatment system |
| CN110316920A (en) * | 2019-07-28 | 2019-10-11 | 南京汉尔斯生物科技有限公司 | A kind of Treatment of Sludge ozone disinfection equipment and its operating method |
| CN111170604A (en) * | 2020-01-19 | 2020-05-19 | 江苏国翔环保科技有限公司 | Ozone sludge treatment equipment and using method thereof |
-
2015
- 2015-04-02 CN CN201520195409.3U patent/CN204607826U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254154A (en) * | 2015-11-24 | 2016-01-20 | 江苏菲德俐环保科技有限公司 | Biochemical sludge reduction integrated equipment |
| CN107721111A (en) * | 2017-11-10 | 2018-02-23 | 北京宜清源科技有限公司 | A kind of system and method for mud decrement processing |
| CN107879583A (en) * | 2017-12-23 | 2018-04-06 | 北京达源环保科技有限公司 | Sludge pyrohydrolysis and anaerobic digestion integrated treatment process system |
| CN110156255A (en) * | 2019-05-10 | 2019-08-23 | 江苏华晖环保科技有限公司 | A kind of hardly possible biochemical waste water advanced treatment system |
| CN110316920A (en) * | 2019-07-28 | 2019-10-11 | 南京汉尔斯生物科技有限公司 | A kind of Treatment of Sludge ozone disinfection equipment and its operating method |
| CN110316920B (en) * | 2019-07-28 | 2020-06-26 | 南京汉尔斯生物科技有限公司 | Ozone disinfection equipment for sludge treatment and operation method thereof |
| CN111170604A (en) * | 2020-01-19 | 2020-05-19 | 江苏国翔环保科技有限公司 | Ozone sludge treatment equipment and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| CB03 | Change of inventor or designer information |
Inventor after: Lang Fei Inventor before: Zhong Chunhong Inventor before: Zheng Hengli |
|
| COR | Change of bibliographic data | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20151026 Address after: 636157, No. 180, Wansheng Road, Xinhua Town, Xuanhan County, Dazhou, Sichuan Patentee after: Lang Fei Address before: A Street South Chengdu Dayuan high tech Zone of Sichuan province 610000 City 1 floor No. 50 Patentee before: CHENGDU LYUYUAN XINCHUANG ENVIRONMENTAL PROTECTION SCIENCE & TECHNOLOGY CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150902 Termination date: 20160402 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |