CN1569698A - Method and equipment for treatment of polluted fluid - Google Patents

Method and equipment for treatment of polluted fluid Download PDF

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Publication number
CN1569698A
CN1569698A CNA2004100182538A CN200410018253A CN1569698A CN 1569698 A CN1569698 A CN 1569698A CN A2004100182538 A CNA2004100182538 A CN A2004100182538A CN 200410018253 A CN200410018253 A CN 200410018253A CN 1569698 A CN1569698 A CN 1569698A
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reactor
bio
contaminated
fluid
case
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CNA2004100182538A
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CN1253388C (en
Inventor
奚旦立
冀世锋
陈季华
茹临锋
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Donghua University
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Donghua University
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Abstract

The invention relates to an apparatus and process for disposing waste water containing organics, nitrogen and phosphor, wherein the apparatus comprises, an anaerobic rotting tank for separating solid substance from the sewage water and waste water, a flow capacity adjustment tank for controlling the load variation of flowing-in waste water, a first, second and third intermittent aeration reaction tank for treating organics, nitrogen and phosphor, a sediment concentration tank for concentrating the solid body and microorganism in the backwashed exhaust, and a drainage tank for sterilizing and draining the water treated by the reaction tank.

Description

A kind of treatment process of contaminated-fluid and equipment thereof
Technical field
The present invention relates to a kind of treatment process and equipment thereof of contaminated-fluid, particularly relate to a kind of biological iron processes-Membrane Bioreactor for Wastewater Treatment method and equipment thereof of contaminated-fluid.
Background technology
Though biochemistry, the physical chemistry method that generally adopts proves a kind of efficient ways at present, but owing to adopt the solid-liquid separation means of gravity type boat davit settling tank as treating water and mud, effluent quality instability often, need tertiary treatment just can reach the reuse water standard, and novel membrane bioreactor combination process has shown very strong advantage, but, seek the important directions that the film pollution prevention technique becomes current membrane bioreactor research because the problem with energy consumption that film pollutes is the common issue with that runs in the membrane bioreactor application.
In order to solve membrane pollution problem, in recent years, all in succession film is polluted control problem both at home and abroad and study.As " Potential and limitations of alum or zeolite addition to improve theperformance of a submerged membrane bioreactor. " " Wat.Sci.Tech " .2001,43 (11): 59-66. has introduced the Korea S scholar alum and zeolite has been added in the submerged membrane bio-reactor, reduced the film pollution, stable effluent quality, but alum has certain toxic action to microflora, and the ammonia nitrogen treatment effect is subjected to obvious influence." adding Powdered Activated Carbon. " " Chinese water supply and drainage " 2001 and for example to the influence of membrane resistance research, 17 (2): 1-4. has reported that active carbon powder adds the preventive and therapeutic effect of having realized in the membrane bioreactor that film pollutes, but the gac cost is higher, need constantly to replenish gac as required in reactor, processing cost improves thereupon.
Yet there are no and be used for wastewater treatment applying biological iron processes and membrane bioreactor bonded equipment and treatment system.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of treatment process and equipment thereof of contaminated-fluid, and the film that exists in the present technology is seriously polluted, floor space is big, cost is high to solve, the unsettled shortcoming of effluent quality.
One of technical problem to be solved by this invention is to provide a kind of treatment process of contaminated-fluid, and this method comprises the steps:
A. iron-based flocculating agent is added in the bio-reactor, domestication forms biological iron mud, and pollution substance is condensed into particle;
B. utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation is 6-15 hour, and sludge age is 20-100 days, and sludge concentration is at 2-10g/L;
C. adopting the aperture is pollution substance in the fibrous filter membrane assembly trap fluid of 0.01 μ m-100 μ m;
D. obtain the cleaning fluid of reuse.
Wherein said iron-based flocculating agent is one or more in ferrous sulfate, ironic hydroxide, poly-ferric chloride or the iron(ic) chloride, and described tunica fibrosa is one or more in polyvinylidene difluoride (PVDF), polyvinyl chloride, polysulfones or the pottery.
The reactor solution concentration of adding to of described iron-based flocculating agent is 5-1000mg/L.
Described contaminated-fluid is for containing in alkali decrement dyeing waste water, starch wastewater or the sanitary wastewater one or more.
Another technical problem to be solved by this invention is to provide a kind of equipment that is used for the contaminated-fluid treatment process, and this equipment comprises water collecting basin, liquid level equilibrium water tank, bio-reactor, intake pump, membrane module, flocculation agent dissolving case, flocculant concentration case and goes out water pump;
Wherein said water collecting basin is located at below ground, described flocculation agent dissolving case, flocculant concentration case bottom pipe is led to bio-reactor, described bio-reactor is positioned at flocculation agent dissolving case, the top of flocculant concentration case, described membrane module is positioned at the inside of bio-reactor, described intake pump links to each other with the liquid level equilibrium case through water intaking valve, and link to each other with bio-reactor through water intaking valve, membrane module communicates with water flow meter and flowing water Valve, connect by the medicament control valve between described flocculation agent dissolving case and the flocculant concentration case, the flocculant concentration case passes through dosing pump, under meter with advance the medicine valve and be connected with bio-reactor.
Described bio-reactor comprises aeration tube, blow-down pipe, blower fan and aeration under meter.
The present invention has advantages such as floor space is little, effluent characteristics good, water conditioning, use is easy to operate, the film pollution is little.Adopt membrane separation technique, integrated suite of equipment with the integrated back invention of main treatment process, add the enhanced flocculation and the biological chemistry treatment effect of biological iron processes, formed and a kind ofly can handle the various wastewater treatment system, reduced film greatly and polluted and reached good effluent quality.
The design is suitable for various wastewater and handles, and the main treatment technology of employing comprises technologies such as materialization coagulation, biological chemistry processing, membrane sepn, biological iron processes.This features on project is to have adopted many new and high technologies, as biological iron processes, pottery or hollow-fibre membrane etc., stable effluent quality, is easy to use operation, is convenient to maintenance.The use of membrane technique makes treat effluent water quality significantly better than treatment process in the past, the solution to membrane pollution problem has effect remarkable especially.
Description of drawings
Fig. 1 is sewage treatment technology process figure;
Fig. 2 is the sewage treatment equipment synoptic diagram.
Among the figure: water collecting basin 1, intake pump 2, liquid level equilibrium case 3, blower fan 4, aeration under meter 5, bio-reactor 6, membrane module 7, aeration tube 8, go out the dissolving of water pump 9, flocculation agent case 10, flocculant concentration case 11, water intaking valve 12, balance control valve 13, tolerance control valve 14, advance medicine valve 15, outlet valve 16, blow-off valve 17, medicament control valve 18, agitator 19, agitator 20, under meter 21, water flow meter 22, dosing pump 23
Embodiment
Below in conjunction with the drawings and specific embodiments the present invention is elaborated.
Embodiment 1.
Adopt following method that starch wastewater is handled:
(1) ferrous sulfate is added in the bio-reactor, strength of solution is 700mg/L in the reactor, and domestication forms biological iron mud, and pollution substance is condensed into particle;
(2) utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation 10 hours, sludge age is 20 days, sludge concentration is stabilized in 7g/L;
(3) adopt polyvinylidene difluoride (PVDF) 0.2 μ m hollow fiber film assembly to filter;
(4) obtain the cleaning fluid of reuse.
Table 1 detection method and standard
Project The measuring method title Measuring method (national standard number)
??pH Glass electrode method ??GB/T6920-1986
Turbidity (NTU) Spectrophotometry ??GB/T13200-1991
??SS(mg/L) Weighting method ??GB/T11901-1989
??COD(mg/L) Dichromate titration ??GB/T11914-1989
??BOD(mg/L) Dilution and inoculation method ??GB/T7488-1987
Total coliform number (individual/L) Plate culture The Drinking Water inspection specification
Chlorine residue N, N-two second class-1,4-phenylenediamine volumetry ??GB/T11897-1989
Table 2 water-quality determination result
Project Example 1
Starch wastewater Handle back water quality
??pH ??7-8 ??6.8-7.5
Turbidity (NTU) ??500- ??2000 ??＜5
??SS(mg/L) ??28-1600 ??＜5
??COD(mg/L) ??650-850 ??25-83
??BOD(mg/L) ??300-450 ??9-20
Embodiment 2.
Adopt following method that dyeing waste water (containing alkali decrement waste water) is handled:
(1) ironic hydroxide is added in the bio-reactor, strength of solution is 175mg/L in the reactor, and domestication forms biological iron mud, and pollution substance is condensed into particle;
(2) utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation 15 hours, sludge age is 20 days, sludge concentration is stabilized in 3.5g/L;
(3) adopt polyvinylidene difluoride (PVDF) 0.2 μ m hollow fiber film assembly to filter;
(4) obtain the cleaning fluid of reuse.
Table 3 water-quality determination result
Project Example 2
Dyeing waste water Handle back water quality
??pH ??8-11 ??6.8-8.5
Turbidity (NTU) ??500- ??2000 ??＜5
??SS(mg/L) ??28-1600 ??＜5
??COD(mg/L) ??600-1000 ??20-80
??BOD(mg/L) ??200-300 ??9-20
Colourity (doubly) ??100-500 ??＜16
Embodiment 3.
Adopt following method that sanitary sewage is handled:
(1) iron(ic) chloride is added in the bio-reactor, 40mg/L in the reactor concentration, domestication forms biological iron mud, and pollution substance is condensed into particle;
(2) utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation 6 hours, sludge age is 100 days, sludge concentration is stabilized in 4g/L;
(3) membrane module adopts polyvinylidene difluoride (PVDF) 0.2 μ m hollow fiber film assembly;
(4) obtain the cleaning fluid of reuse.
Table 4 water-quality determination result
Project Example 3 The limit value of miscellaneous domestic water quality standard (GJ25.1-89) regulation
Sanitary sewage Handle back water quality
?pH ??6.7-6.8 ??6.8-6.9 ??6.5-9.0
Turbidity (NTU) ??500- ??2000 ??＜5 ??5
?SS(mg/L) ??28-1600 ??＜5 ??5
?COD(mg/L) ??80-320 ??12-39 ??50
?BOD(mg/L) ??26-68 ??3-10 ??10
Total coliform number (individual/L) ??20-1000 Do not detect ??3
Chlorine residue ??- ??2.0-3.0 The terminal water of pipe network is not less than 0.2
Embodiment 4.
Adopt following method that cotton spinning (reactive dyestuffs) dyeing waste water is handled:
(1) poly-ferric chloride is added in the bio-reactor, concentration is 450mg/L in the reactor, and domestication forms biological iron mud, and pollution substance is condensed into particle;
(2) utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation 9 hours, sludge age is 100 days, sludge concentration is stabilized in 9g/L;
(3) membrane module adopts polyvinylidene difluoride (PVDF) 0.2 μ m hollow fiber film assembly;
(4) obtain the cleaning fluid of reuse.
Table 5 water-quality determination result
Project Example 4
Dyeing waste water Handle back water quality
??pH ??8-11 ??6.8-6.9
Turbidity (NTU) ??500- ??2000 ??＜5
??SS(mg/L) ??28-1600 ??＜5
??COD(mg/L) ??600-850 ??30-70
??BOD(mg/L) ??150-250 ??14-30
Colourity (degree) ??100-500 ??＜16
Embodiment 5
A kind of equipment that is used for the contaminated-fluid treatment process, this equipment comprise water collecting basin 1, liquid level equilibrium case 3, bio-reactor 6, intake pump 2, membrane module 7, flocculation agent dissolving case 10, flocculant concentration case 11 and go out water pump 9;
Wherein water collecting basin 1 is located at below ground, flocculation agent dissolving case 10, flocculant concentration case 11 bottom pipe are led to bio-reactor 6, bio-reactor 6 is positioned at flocculation agent dissolving case 10, the top of flocculant concentration case 11, membrane module 7 is positioned at the inside of bio-reactor, intake pump 2 links to each other with liquid level equilibrium case 3 through water intaking valve 12, and link to each other with bio-reactor 6 through water intaking valve 12, membrane module 7 communicates with water flow meter 22 and flowing water Valve 16, connect by medicament control valve 18 between flocculation agent dissolving case 10 and the flocculant concentration case 11, flocculant concentration case 11 is by dosing pump 23, under meter 21 with advance medicine valve 15 and be connected with bio-reactor 6.Bio-reactor 6 comprises aeration tube 8, blow-down pipe 17, blower fan 4 and aeration under meter 5.

Claims (8)

1. the treatment process of a contaminated-fluid is characterized in that this method comprises the steps:
A. iron-based flocculating agent is added in the bio-reactor, domestication forms biological iron mud, and pollution substance is condensed into particle;
B. utilize the active sludge in the bio-reactor to carry out biochemical action, remove the pollution substance in the contaminated-fluid, the hydraulic detention time of operation is 6-15 hour, and sludge age is 20-100 days, and sludge concentration is at 2-10g/L;
C. adopting the aperture is pollution substance in the fibrous filter membrane assembly trap fluid of 0.01 μ m-100 μ m;
D. obtain the cleaning fluid of reuse.
2. the treatment process of contaminated-fluid according to claim 1, it is characterized in that described iron-based flocculating agent is one or more in ferrous sulfate, ironic hydroxide, poly-ferric chloride or the iron(ic) chloride, described tunica fibrosa is one or more in polyvinylidene difluoride (PVDF), polyvinyl chloride, polysulfones or the pottery.
3. the treatment process of contaminated-fluid according to claim 1 is characterized in that described contaminated-fluid is for containing in alkali decrement dyeing waste water, starch wastewater or the sanitary wastewater one or more.
4. the treatment process of contaminated-fluid according to claim 1 is characterized in that described iron-based flocculating agent is one or more in ferrous sulfate, ironic hydroxide, poly-ferric chloride or the iron(ic) chloride.
5. the treatment process of contaminated-fluid according to claim 1 is characterized in that described tunica fibrosa is one or more in polyvinylidene difluoride (PVDF), polyvinyl chloride, polysulfones or the pottery.
6. the treatment process of contaminated-fluid according to claim 1 is characterized in that it is 5-1000mg/L that described iron-based flocculating agent adds reactor concentration to.
7. an equipment that is used for as each described contaminated-fluid treatment process of claim 1～6 is characterized in that this equipment comprises water collecting basin (1), liquid level equilibrium case (3), bio-reactor (6), intake pump (2), membrane module (7), flocculation agent dissolving case (10), flocculant concentration case (11) and goes out water pump (9);
Wherein said water collecting basin (1) is located at below ground, described flocculation agent dissolving case (10), flocculant concentration case (11) bottom pipe is led to bio-reactor (6), described bio-reactor (6) is positioned at flocculation agent dissolving case (10), the top of flocculant concentration case (11), described membrane module (7) is positioned at the inside of bio-reactor, described intake pump (2) links to each other with liquid level equilibrium case (3) through water intaking valve (12), and link to each other with bio-reactor (6) through water intaking valve (12), membrane module (7) communicates with water flow meter (22) and flowing water Valve (16), connect by medicament control valve (18) between described flocculation agent dissolving case (10) and the flocculant concentration case (11), flocculant concentration case (11) is by dosing pump (23), under meter (21) with advance medicine valve (15) and be connected with bio-reactor (6).
8. the equipment that is used for the contaminated-fluid treatment process according to claim 7 is characterized in that described bio-reactor (6) comprises aeration tube (8), blow-down pipe (17), blower fan (4) and aeration under meter (5).
CNB2004100182538A 2004-05-12 2004-05-12 Method and equipment for treatment of polluted fluid Expired - Fee Related CN1253388C (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101609309B (en) * 2009-07-11 2011-03-23 大连理工大学 Membrane pollution optimized control specialist system of membrane reactor
CN101538107B (en) * 2009-05-12 2011-07-20 青岛银河环保股份有限公司 Method for treating wastewater in textile printing and dyeing industry
CN101665291B (en) * 2009-09-27 2011-08-10 范兆科 Method of realizing zero emission by advanced treatment and reuse of dyeing waste water
CN1872734B (en) * 2005-06-01 2011-08-24 纳尔科公司 A method for improving flux in a membrane bioreactor
WO2011120192A1 (en) * 2010-03-31 2011-10-06 General Electric Company (A New York Corporation) Methods of conditioning mixed liquor using water soluble quaternary ammonium starches
CN101426565B (en) * 2004-04-22 2012-04-18 西门子工业公司 Filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials
CN101462793B (en) * 2009-01-14 2012-05-30 青岛理工大学 Method for promoting denitrification and dephosphorization of activated sludge sewerage by using composite iron enzyme
CN102502949A (en) * 2011-11-02 2012-06-20 青岛理工大学 Method for improving activity of nitrification function microbiology in activated sludge through feeding iron hydroxide during in situ preparation
CN102648162A (en) * 2009-10-06 2012-08-22 悉尼科技大学 Method for enhancing biological water treatment
CN104049565A (en) * 2014-05-26 2014-09-17 范振捷 Method for controlling industrial wastewater level
CN106587509A (en) * 2016-12-28 2017-04-26 苏州首创嘉净环保科技股份有限公司 Garbage press filtrate treatment device
CN107986522A (en) * 2017-11-22 2018-05-04 苏州雷沃克环保科技有限公司 A kind of wastewater purification technique

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101426565B (en) * 2004-04-22 2012-04-18 西门子工业公司 Filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials
CN1872734B (en) * 2005-06-01 2011-08-24 纳尔科公司 A method for improving flux in a membrane bioreactor
CN101462793B (en) * 2009-01-14 2012-05-30 青岛理工大学 Method for promoting denitrification and dephosphorization of activated sludge sewerage by using composite iron enzyme
CN101538107B (en) * 2009-05-12 2011-07-20 青岛银河环保股份有限公司 Method for treating wastewater in textile printing and dyeing industry
CN101609309B (en) * 2009-07-11 2011-03-23 大连理工大学 Membrane pollution optimized control specialist system of membrane reactor
CN101665291B (en) * 2009-09-27 2011-08-10 范兆科 Method of realizing zero emission by advanced treatment and reuse of dyeing waste water
CN102648162A (en) * 2009-10-06 2012-08-22 悉尼科技大学 Method for enhancing biological water treatment
WO2011120192A1 (en) * 2010-03-31 2011-10-06 General Electric Company (A New York Corporation) Methods of conditioning mixed liquor using water soluble quaternary ammonium starches
CN102892715A (en) * 2010-03-31 2013-01-23 通用电气公司 Methods of conditioning mixed liquor using water soluble quaternary ammonium starches
US8778185B2 (en) 2010-03-31 2014-07-15 General Electric Company Methods of conditioning mixed liquor using water soluble quaternary ammonium starches
CN102502949A (en) * 2011-11-02 2012-06-20 青岛理工大学 Method for improving activity of nitrification function microbiology in activated sludge through feeding iron hydroxide during in situ preparation
CN104049565A (en) * 2014-05-26 2014-09-17 范振捷 Method for controlling industrial wastewater level
CN106587509A (en) * 2016-12-28 2017-04-26 苏州首创嘉净环保科技股份有限公司 Garbage press filtrate treatment device
CN107986522A (en) * 2017-11-22 2018-05-04 苏州雷沃克环保科技有限公司 A kind of wastewater purification technique

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