CN103086479A - High-efficiency energy-saving sewage treatment device - Google Patents
High-efficiency energy-saving sewage treatment device Download PDFInfo
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- CN103086479A CN103086479A CN2013100246882A CN201310024688A CN103086479A CN 103086479 A CN103086479 A CN 103086479A CN 2013100246882 A CN2013100246882 A CN 2013100246882A CN 201310024688 A CN201310024688 A CN 201310024688A CN 103086479 A CN103086479 A CN 103086479A
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Abstract
The invention discloses a high-efficiency energy-saving sewage treatment device which comprises a storage chamber (1), an electrocatalytic oxidation chamber (2) and a depth purifying chamber (4), wherein the storage chamber is communicated with the electrocatalytic oxidation chamber (2); the electrocatalytic oxidation chamber (2) is communicated with the depth purifying chamber (4); a sewage inlet is communicated with the storage chamber (1); the depth purifying chamber (4) is communicated with a water outlet; a crushing pump (6) is arranged on a connection pipeline between the storage chamber (1) and the electrocatalytic oxidation chamber (2); a discharging pump (7) is arranged on a connection pipeline between the depth purifying chamber (4) and the water outlet; a liquid level controller is respectively arranged inside the storage chamber (1) and the depth purifying chamber (4) to control the starting of the crushing pump (6) and the discharging pump (7). The high-efficiency energy-saving sewage treatment device provided by the invention carries out oxydative degradation by conducting choiceless rapid chain reaction between strong oxidation particles generated in the electrocatalytic oxidation reaction process and organic pollutants in wastewater.
Description
Technical field
The present invention relates to a kind of energy-efficient waste disposal plant, for the treatment of various Heisui River and the buck from boats and ships, make it rear any discharging up to standard.
Background technology
A series of biochemical actions can occur in the unprocessed water surrounding that enters arbitrarily of Sewage from Ships: natural purification process and the eubiosis that 1, can destroy water surrounding; 2, cause the dead or migration of the animals such as fish in water surrounding; 3, can make algae excessive ground Growth and reproduction, eutrophication occur; 4, the resource generation in bathing beach and fishing ground seriously influenced; 5, spread disease, can produce threat to the mankind's health.At present, process main biological degradation method and the physico-chemical processes of adopting for the organic pollutant in sewage, biological degradation method is processed sanitary sewage and is most widely used at present, but have more difficult removal biological degradation organism, be subjected to the microorganism growth characteristic limitations, the problems such as the biological domestication time is long.Physical chemistry need to add the medicines such as flocculation agent, oxygenant, technical process complexity, the bad processing of regeneration waste liquid, easily causes secondary pollution etc.the above-mentioned shortcoming of biological degradation method and physico-chemical processes, certainly will cause the waste disposal plant handling property low, machine volume is large, working cost is high, level of automation is low, can be widely used in the municipal sewage plant at present, because sewage work can not be subjected to the space, time and personnel's restriction, yet the mobile platform such as oil platform and marine ship, requirement to equipment such as waste disposal plants is that volume is little, lightweight, level of automation is high, need not routine maintenance, thereby no matter adopt biological degradation method or physico-chemical processes all can't realize, use range and the effect of waste disposal plant have all been limited.
Summary of the invention
In order to address the above problem, the invention provides a kind of energy-efficient waste disposal plant, utilize the strong oxidic particle that generates in the electrolytic catalysis reaction process, without chain reaction selectively occurs fast, carry out oxidative degradation with organic pollutant in waste water.
the present invention has adopted following technical scheme: a kind of energy-efficient waste disposal plant, it comprises storage chamber, the catalytic oxidation chamber, the deep purifying chamber, described storage chamber is communicated with by connecting pipeline with the catalytic oxidation chamber, described catalytic oxidation chamber is communicated with by connecting pipeline with the deep purifying chamber, sewage inlet is communicated with storage chamber by connecting pipeline, the deep purifying chamber is communicated with water outlet by connecting pipeline, connecting pipeline between described storage chamber and catalytic oxidation chamber is provided with macerator pump, connecting pipeline between described deep purifying chamber and water outlet is provided with emptying pump, be respectively equipped with a fluid level controller in described storage chamber and deep purifying chamber, the fluid level controller in storage chamber is controlled the startup of macerator pump, the startup of the fluid level controller control emptying pump in the deep purifying chamber.
One side of described storage chamber is provided with air pump, and storage chamber is connected with air pump by the aeration tube of bottom; The bottom in described catalytic oxidation chamber is provided with the residue collecting chamber, and the bottom in catalytic oxidation chamber is communicated with by connecting pipeline with the residue collecting chamber, and this connecting pipeline is provided with valve V5; The bottom in described deep purifying chamber is provided with return line the deep purifying chamber is communicated with connecting pipeline between storage chamber and macerator pump; Described return line is provided with valve V4 and valve V7, and described valve V4 and valve V7 lay respectively at the two ends of return line; Connecting pipeline between described sewage inlet and storage chamber is provided with valve V2, and the connecting pipeline between described storage chamber and macerator pump is provided with valve V3, and the connecting pipeline between described catalytic oxidation chamber and deep purifying chamber is provided with V6; One side of described storage chamber is provided with by-pass line, and this by-pass line is provided with valve V1.
The advantages such as the present invention has following beneficial effect: the present invention has efficient sterilizing, and soil release characteristics is strong are not added any medicament, and whole process is completed in equipment, have reduced the risk of storage and the artificial dispensing of medicine; Compact construction, volume are little, simple installation, and easy care is fit to be arranged on all size boats and ships; Simple to operate, reliable, need not personnel's nurse, be more suitable in the unmanned engine room; Can be used in buck and Heisui River on various ships, energy consumption is low, energy-conserving and environment-protective.
Description of drawings
Fig. 1 is structural representation of the present invention.
Embodiment
as shown in Figure 1, a kind of energy-efficient waste disposal plant, it comprises storage chamber 1, catalytic oxidation chamber 2, deep purifying chamber 4, described storage chamber 1 is communicated with by connecting pipeline with catalytic oxidation chamber 2, described catalytic oxidation chamber 2 is communicated with by connecting pipeline with deep purifying chamber 4, sewage inlet is communicated with storage chamber 1 by connecting pipeline, deep purifying chamber 4 is communicated with water outlet by connecting pipeline, connecting pipeline between described storage chamber 1 and catalytic oxidation chamber 2 is provided with macerator pump 6, connecting pipeline between described deep purifying chamber 4 and water outlet is provided with emptying pump 7, be respectively equipped with a fluid level controller in described storage chamber 1 and deep purifying chamber 4, the fluid level controller in storage chamber 1 is controlled the startup of macerator pump 6, and the fluid level controllers in deep purifying chamber 4 are controlled the startup of emptying pump 7, one side of described storage chamber 1 is provided with air pump 5, and storage chamber 1 is connected with air pump 5 by the aeration tube of bottom, the bottom in described catalytic oxidation chamber 2 is provided with residue collecting chamber 3, and the bottom in catalytic oxidation chamber 2 is communicated with by connecting pipeline with residue collecting chamber 3, and this connecting pipeline is provided with valve V5, the bottom in described deep purifying chamber 4 is provided with return line deep purifying chamber 4 is communicated with connecting pipeline between storage chamber 1 and macerator pump 6, described return line is provided with valve V4 and valve V7, and described valve V4 and valve V7 lay respectively at the two ends of return line, connecting pipeline between described sewage inlet and storage chamber 1 is provided with valve V2, and the connecting pipeline between described storage chamber 1 and macerator pump 6 is provided with valve V3, and the connecting pipeline between described catalytic oxidation chamber 2 and deep purifying chamber 4 is provided with V6, one side of described storage chamber 1 is provided with by-pass line, and this by-pass line is provided with valve V1.
At first the sewage of locating from lavatory, clinic etc. when the present invention uses enter storage chamber, and storage chamber bottom is furnished with aeration tube and is connected with air pump, and sewage enters rear air pump work, make in storage chamber sewage constantly rolling deposit being unlikely to; When the sewage in storage chamber reached certain liquid level, macerator pump started, and sewage is rejected to the catalytic oxidation chamber, reject in process in sewage the macrobead thing and fully pulverized, thereby the sewage that enters the catalytic oxidation chamber almost becomes flocculence; In the catalytic oxidation chamber, the strong oxidation activity species that the effect by electrode and catalytic material produces carry out oxidative degradation to the organism in sewage, make it be degraded to carbonic acid gas, water and simple low molecule organic matter; Intimate primary water after oxidative degradation flows into the deep purifying chamber, abundant precipitate and separate in the deep purifying chamber, and when liquid level reach a certain height, emptying pump started, and the water after up to standard is discharged outboard.After the device long-play, bottom, catalytic oxidation chamber can deposit a little inorganics that can't degrade, when macerator pump quits work, opens valve V5, and the bottom settlings thing is entered the residue collecting chamber, collects pending.Affect water quality for avoiding bottom, deep purifying chamber to form alluvial, be provided with return line in its bottom and macerator pump entrance, in the discharge water precipitation process, throw out is pumped to the catalytic oxidation chamber degradation treatment again by macerator pump.When boats and ships walk to specified sea areas or long-term landing pier, when sewage need not to process through device, but valve-off V2, open valve V1, discharge boats and ships by by-pass line, during the device normal operation, valve V2, V3, V6 often open, valve V4, V7 are crack, and the start and stop of air pump, macerator pump and emptying pump are controlled by fluid level controller.
Claims (7)
1. energy-efficient waste disposal plant, it is characterized in that it comprises storage chamber (1), catalytic oxidation chamber (2), deep purifying chamber (4), described storage chamber (1) is communicated with by connecting pipeline with catalytic oxidation chamber (2), described catalytic oxidation chamber (2) is communicated with by connecting pipeline with deep purifying chamber (4), sewage inlet is communicated with storage chamber (1) by connecting pipeline, deep purifying chamber (4) is communicated with water outlet by connecting pipeline, connecting pipeline between described storage chamber (1) and catalytic oxidation chamber (2) is provided with macerator pump (6), connecting pipeline between described deep purifying chamber (4) and water outlet is provided with emptying pump (7), be respectively equipped with a fluid level controller in described storage chamber (1) and deep purifying chamber (4), the fluid level controller in storage chamber (1) is controlled the startup of macerator pump (6), and the fluid level controller in deep purifying chamber (4) is controlled the startup of emptying pump (7).
2. a kind of energy-efficient waste disposal plant according to claim 1, is characterized in that a side of described storage chamber (1) is provided with air pump (5), and storage chamber (1) is connected with air pump (5) by the aeration tube of bottom.
3. a kind of energy-efficient waste disposal plant according to claim 1, the bottom that it is characterized in that described catalytic oxidation chamber (2) is provided with residue collecting chamber (3), the bottom in catalytic oxidation chamber (2) is communicated with by connecting pipeline with residue collecting chamber (3), and this connecting pipeline is provided with valve V5.
4. a kind of energy-efficient waste disposal plant according to claim 1, the bottom that it is characterized in that described deep purifying chamber (4) are provided with return line deep purifying chamber (4) are communicated with connecting pipeline between storage chamber (1) and macerator pump (6).
5. a kind of energy-efficient waste disposal plant according to claim 4, is characterized in that described return line is provided with valve V4 and valve V7, and described valve V4 and valve V7 lay respectively at the two ends of return line.
6. a kind of energy-efficient waste disposal plant according to claim 1, it is characterized in that the connecting pipeline between described sewage inlet and storage chamber (1) is provided with valve V2, connecting pipeline between described storage chamber (1) and macerator pump (6) is provided with valve V3, and the connecting pipeline between described catalytic oxidation chamber (2) and deep purifying chamber (4) is provided with V6.
7. a kind of energy-efficient waste disposal plant according to claim 1, is characterized in that a side of described storage chamber (1) is provided with by-pass line, and this by-pass line is provided with valve V1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013100246882A CN103086479A (en) | 2013-01-23 | 2013-01-23 | High-efficiency energy-saving sewage treatment device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2013100246882A CN103086479A (en) | 2013-01-23 | 2013-01-23 | High-efficiency energy-saving sewage treatment device |
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| CN103086479A true CN103086479A (en) | 2013-05-08 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030413A (en) * | 2014-05-17 | 2014-09-10 | 曹学良 | Treatment device for electrocatalytic oxidation of ship domestic sewage and method thereof |
| CN108892335A (en) * | 2018-09-05 | 2018-11-27 | 武汉船舶职业技术学院 | A kind of processing system and its processing method in ship processing oil-containing waste water for ship |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101068751A (en) * | 2005-08-26 | 2007-11-07 | 埃瓦克股份有限公司 | Method for oxidative treatment of aqueous liquids |
| CN201770560U (en) * | 2010-08-13 | 2011-03-23 | 宁波四通金属制品有限公司 | Ship sewage treatment device |
| CN202297302U (en) * | 2011-09-30 | 2012-07-04 | 玄明环保科技（上海）有限公司 | Membrane-method treatment device for domestic sewage |
| CN202379836U (en) * | 2011-11-30 | 2012-08-15 | 青岛双瑞海洋环境工程股份有限公司 | Composite type sanitary sewage treatment system for ships |
-
2013
- 2013-01-23 CN CN2013100246882A patent/CN103086479A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101068751A (en) * | 2005-08-26 | 2007-11-07 | 埃瓦克股份有限公司 | Method for oxidative treatment of aqueous liquids |
| CN201770560U (en) * | 2010-08-13 | 2011-03-23 | 宁波四通金属制品有限公司 | Ship sewage treatment device |
| CN202297302U (en) * | 2011-09-30 | 2012-07-04 | 玄明环保科技（上海）有限公司 | Membrane-method treatment device for domestic sewage |
| CN202379836U (en) * | 2011-11-30 | 2012-08-15 | 青岛双瑞海洋环境工程股份有限公司 | Composite type sanitary sewage treatment system for ships |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104030413A (en) * | 2014-05-17 | 2014-09-10 | 曹学良 | Treatment device for electrocatalytic oxidation of ship domestic sewage and method thereof |
| CN108892335A (en) * | 2018-09-05 | 2018-11-27 | 武汉船舶职业技术学院 | A kind of processing system and its processing method in ship processing oil-containing waste water for ship |
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Application publication date: 20130508 |