CN107986580A - A kind of aquaculture wastewater processing system - Google Patents

A kind of aquaculture wastewater processing system Download PDF

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Publication number
CN107986580A
CN107986580A CN201711485085.7A CN201711485085A CN107986580A CN 107986580 A CN107986580 A CN 107986580A CN 201711485085 A CN201711485085 A CN 201711485085A CN 107986580 A CN107986580 A CN 107986580A
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China
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unit
plate
tubular
sewage
aquaculture wastewater
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CN201711485085.7A
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CN107986580B (en
Inventor
吕瑞霞
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Dongguan Jianyuanquan Water Treatment Technology Co ltd
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Mr Lin Of Hangzhou Environmental Protection Technology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46133Electrodes characterised by the material
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46152Electrodes characterised by the shape or form
    • C02F2001/46171Cylindrical or tubular shaped
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/16Nitrogen compounds, e.g. ammonia
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/46125Electrical variables
    • C02F2201/4614Current
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/4612Controlling or monitoring
    • C02F2201/4615Time
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/08Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/44Time
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/284Anaerobic digestion processes using anaerobic baffled reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2866Particular arrangements for anaerobic reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

The invention discloses a kind of aquaculture wastewater processing system, including deamination pretreatment unit, tubular reactor unit and wetland variation unit, each unit to be sequentially connected with;The tubular reactor unit is wholely set using Anaerobic Treatment unit and tubular plate processing unit, and leading portion is Anaerobic Treatment unit, and rear end is tubular plate processing unit;The tubular reactor unit is provided with centre rotational axis, the surrounding of Anaerobic Treatment unit center rotation axis is provided with filler, centre rotational axis drive filler rotation;The centre rotational axis of tubular plate processing section are provided with blade, the blade of rotary motion drives current to disturb up and down, the tubular reactor includes the anode plate and cathode plate laid up and down, the anode plate and cathode plate fitting tube wall is set, and solves the technical problem that efficiency is low, processing cost is high in aquaculture wastewater processing procedure and takes up a large area.

Description

A kind of aquaculture wastewater processing system
Technical field
The invention belongs to sewage treatment field, more particularly to a kind of processing system of aquaculture wastewater.
Background technology
China is agricultural production big country, and in recent years, livestock and poultry cultivation scale constantly expands, and aquaculture wastewater is rich in nitrogen, phosphorus, organic Thing, directly discharge can impact environment.Livestock and poultry breeding scale pollution prevention ordinance points out that Animal Raising Zone should be built accordingly Feces of livestock and poultry, sewage treatment facility.Anaerobic digestion is the processing common method of feces of livestock and poultry, can not only realize livestock and poultry cultivation The harmless treatment of discarded object, can also provide biogas as clean energy resource.With the fast development of biogas engineering, largely Biogas slurry also produces therewith.It is also far from enough to qualified discharge but anaerobic digestion is merely capable of the pretreatment as initial stage.Poultry Fowl aquaculture wastewater/biogas slurry unit volume nutrient content is low, and storage, cost of transportation are higher, with the development of membrane separation technique, poultry Fowl aquaculture wastewater/biogas slurry film concentration technique becomes the hot spot of research.Livestock and poultry cultivation sewage/biogas slurry is after UF membrane, concentrate Liquid organic fertilizer can be configured, permeate can be with reuse.In practical applications, the expense of film account for whole system cost 5%~ 30%, the suspended matter, colloidal content in livestock and poultry cultivation sewage/biogas slurry are higher, can cause serious fouling membrane, it is concentrated in film Before, feed liquid is pre-processed.Although processing of the film process to aquaculture wastewater has good effect, long-play The processing cost that fouling membrane is brought is very high, this is difficult to bear for common farm.
The content of the invention
In view of the above problems, the present invention provides a kind of sewage disposal system of aquaculture wastewater, solves aquaculture wastewater and treats The technical problem that efficiency is low in journey, processing cost is high and takes up a large area.
The present invention provides a kind of sewage disposal system of aquaculture wastewater, it is characterised in that:It is single that it includes deamination pretreatment Member 1, tubular reactor unit 2 and wetland variation unit 3, above-mentioned processing unit are sequentially connected with;The deamination pretreatment unit Using baffle plate type deammoniation tower 11, treatment sewage is flowed from above to below from tower top, and in tower wall both sides, setting is staggered multiple Baffle plate 12, is provided with hot air apparatus 13 in the tower wall between baffle plate, is imported hot wind by hot air apparatus 13 each adjacent Baffle plate 12 between;Treatment sewage drops into the beginning of next baffle plate from the end of a upper baffle plate, so that shape Flowed into S-shaped;The density of setting of the baffle plate gradually increases from top to bottom.
The tubular reactor unit 2 is wholely set using Anaerobic Treatment unit 21 and tubular plate processing unit 22, preceding Section is Anaerobic Treatment unit, and rear end is tubular plate processing unit;The tubular reactor unit is provided with centre rotational axis 23, The surrounding of Anaerobic Treatment unit center rotation axis is provided with filler 24, centre rotational axis 23 drive filler 24 to rotate;In tubular type The centre rotational axis of pole plate processing unit are provided with blade 25, and the blade of rotary motion drives current to disturb up and down, the tubular type Reactor includes the positive plate 26 and minus plate 27 laid up and down, and positive plate 26 and minus plate 27 the fitting tube wall is set.
Preferably, the deamination pretreatment unit tower top is provided with air outlet, tower body a height of 3m, diameter 1m, baffle plate The spacing of end and tower wall is 0.3m;
Preferably, the long 5m of the tubular reactor, diameter 0.5m, wherein Anaerobic Treatment unit 21 and tubular plate processing unit 22 Respectively 2.5m, 2.5m;
The anode of the tubular plate processing unit is using platinum electrode, lead dioxide electrode;
Preferably, residence time 30-60 minute of deamination pretreatment unit.
Beneficial effects of the present invention:
(1)By the baffle plate being staggered, ensure the residence time of aquaculture wastewater, and the density of setting of baffle plate is not uniform , by reasonably setting the density of baffle plate to ensure that the efficiency of removal of ammonia and nitrogen, baffle(s) spacing, which is set, ensures ammonia as early as possible Reach tower top air outlet.
(2)Tubular reactor is wholely set, and centre rotational axis provide power for two processing units at the same time, can not only band Dynamic filler so that aging sludge comes off, and causes the sewage of tubular plate reactor to form disturbance, ensures wastewater electrochemical treatment place The high efficiency of reason.
(3)The present invention ensure that rural area by the combination of anaerobic baffled reaction device, tubular reactor and wetland variation The efficient process of aquaculture wastewater, especially suitable for the remote districts of sewage treatment plant's centralized processing are not implemented.
Brief description of the drawings
Fig. 1 is the schematic diagram of the processing system of aquaculture wastewater.
Embodiment
Embodiment 1
Sewage of farm COD2000mg/L, is flowed from above to below the top of sewage lifting to deammoniation tower, sewage by water pump, Sewage is in the residence time 1h of deamination pretreatment unit, and sewage flows into anaerobic pretreatment unit from bottom of towe, and sewage locates in advance in anaerobism Unit residence time 0.5h is managed, the water outlet of anaerobic pretreatment unit enters tubular plate processing unit, and sewage is in tubular plate processing The residence time 0.5h of unit, current density 15mA/cm2, water outlet enter wetland variation unit, and the COD after processing is reduced to 30mg/L。
Embodiment 2
Sewage of farm COD2000mg/L, is flowed from above to below the top of sewage lifting to deammoniation tower, sewage by water pump, Sewage is in the residence time 1h of deamination pretreatment unit, and sewage flows into anaerobic pretreatment unit from bottom of towe, and sewage locates in advance in anaerobism Unit residence time 0.5h is managed, the water outlet of anaerobic pretreatment unit enters tubular plate processing unit, and sewage is in tubular plate processing The residence time 0.5h of unit, current density 25mA/cm2, water outlet enter wetland variation unit, and the COD after processing is reduced to 25mg/L。
Embodiment 3
Sewage of farm COD3000mg/L, is flowed from above to below the top of sewage lifting to deammoniation tower, sewage by water pump, Sewage is in the residence time 1h of deamination pretreatment unit, and sewage flows into anaerobic pretreatment unit from bottom of towe, and sewage locates in advance in anaerobism Unit residence time 0.5h is managed, the water outlet of anaerobic pretreatment unit enters tubular plate processing unit, and sewage is in tubular plate processing The residence time 0.5h of unit, current density 15mA/cm2, water outlet enter wetland variation unit, and the COD after processing is reduced to 40mg/L。
Embodiment 4
Sewage of farm COD3000mg/L, is flowed from above to below the top of sewage lifting to deammoniation tower, sewage by water pump, Sewage is in the residence time 1h of deamination pretreatment unit, and sewage flows into anaerobic pretreatment unit from bottom of towe, and sewage locates in advance in anaerobism Unit residence time 0.5h is managed, the water outlet of anaerobic pretreatment unit enters tubular plate processing unit, and sewage is in tubular plate processing The residence time 0.5h of unit, current density 20mA/cm2, water outlet enter wetland variation unit, and the COD after processing is reduced to 30mg/L。
Embodiment 5
Sewage of farm COD5000mg/L, is flowed from above to below the top of sewage lifting to deammoniation tower, sewage by water pump, Sewage is in the residence time 1h of deamination pretreatment unit, and sewage flows into anaerobic pretreatment unit from bottom of towe, and sewage locates in advance in anaerobism Unit residence time 0.5h is managed, the water outlet of anaerobic pretreatment unit enters tubular plate processing unit, and sewage is in tubular plate processing The residence time 1h of unit, current density 15mA/cm2, water outlet enter wetland variation unit, and the COD after processing is reduced to 50mg/ L。

Claims (6)

  1. A kind of 1. aquaculture wastewater processing system, it is characterised in that:It include deamination pretreatment unit, tubular reactor unit and Wetland variation unit, each unit are sequentially connected with;The tubular reactor unit is handled using Anaerobic Treatment unit and tubular plate Unit is wholely set, and leading portion is Anaerobic Treatment unit, and rear end is tubular plate processing unit;The tubular reactor unit is set There are centre rotational axis, the surrounding of Anaerobic Treatment unit center rotation axis is provided with filler, centre rotational axis drive filler rotation; The centre rotational axis of tubular plate processing section are provided with blade, the blade of rotary motion drives current to disturb up and down, the pipe Formula reactor includes the anode plate and cathode plate laid up and down, and the anode plate and cathode plate fitting tube wall is set.
  2. 2. aquaculture wastewater processing system as claimed in claim 1, it is characterised in that:The deamination pretreatment unit uses baffling Board-like deammoniation tower, treatment sewage are flowed from above to below from tower top, and multiple baffle plates that are staggered, baffling are set in tower wall both sides Hot air apparatus is provided with tower wall between plate, is imported hot wind between each adjacent baffle plate by hot air apparatus;Wait to locate Reason sewage drops into the beginning of next baffle plate from the end of a upper baffle plate, so as to form S-shaped flowing;The baffle plate Density of setting gradually increase from top to bottom.
  3. 3. aquaculture wastewater processing system as claimed in claim 2, it is characterised in that:The deamination pretreatment unit tower top is set There is air outlet, a height of 3m of tower body, diameter 1m, the end of baffle plate and the spacing of tower wall are 0.3m;Wherein, bottom baffle plate with Layer baffle plate second from the bottom is up incremented by intervals of 0.2m, adjacent baffle plate interval with 0.1m.
  4. 4. aquaculture wastewater processing system as claimed in claim 2, it is characterised in that:The long 5m of tubular reactor unit, directly Footpath 0.5m, wherein Anaerobic Treatment unit 21 and tubular plate processing unit 22 are respectively 2.5m, 2.5m.
  5. 5. aquaculture wastewater processing system as claimed in claim 2, it is characterised in that:The anode of the tubular plate processing unit Using platinum electrode, lead dioxide electrode.
  6. 6. aquaculture wastewater processing system as claimed in claim 2, it is characterised in that:When the sewage of deamination pretreatment unit stops Between 30-60 minutes.
CN201711485085.7A 2017-12-30 2017-12-30 Culture sewage treatment system Active CN107986580B (en)

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Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1903752A (en) * 2005-07-28 2007-01-31 中国环境科学研究院 Method of nitrosation electrochemical back nitrosation full autotrophic deammoniacal nitrogen and its reactor
CN101774724A (en) * 2009-01-14 2010-07-14 上海博丹环境工程技术有限公司 Method for treating production wastewater of glucide
CN102897979A (en) * 2012-10-23 2013-01-30 鞍钢股份有限公司 Coking wastewater treatment method
CN103288302A (en) * 2013-06-27 2013-09-11 波鹰(厦门)科技有限公司 Livestock/poultry breeding wastewater resource utilization and treatment device
CN104860362A (en) * 2014-02-21 2015-08-26 江苏夏航环境工程有限公司 Concentrated ammonia rectification apparatus for treating titanium dioxide industrial wastewater
CN204848572U (en) * 2015-07-03 2015-12-09 绵阳科勤环保科技有限公司 Birds is raised and grows effluent treatment plant
CN107082528A (en) * 2017-04-19 2017-08-22 长江大学 A kind of livestock breeding wastewater advanced treatment process

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1903752A (en) * 2005-07-28 2007-01-31 中国环境科学研究院 Method of nitrosation electrochemical back nitrosation full autotrophic deammoniacal nitrogen and its reactor
CN101774724A (en) * 2009-01-14 2010-07-14 上海博丹环境工程技术有限公司 Method for treating production wastewater of glucide
CN102897979A (en) * 2012-10-23 2013-01-30 鞍钢股份有限公司 Coking wastewater treatment method
CN103288302A (en) * 2013-06-27 2013-09-11 波鹰(厦门)科技有限公司 Livestock/poultry breeding wastewater resource utilization and treatment device
CN104860362A (en) * 2014-02-21 2015-08-26 江苏夏航环境工程有限公司 Concentrated ammonia rectification apparatus for treating titanium dioxide industrial wastewater
CN204848572U (en) * 2015-07-03 2015-12-09 绵阳科勤环保科技有限公司 Birds is raised and grows effluent treatment plant
CN107082528A (en) * 2017-04-19 2017-08-22 长江大学 A kind of livestock breeding wastewater advanced treatment process

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