• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The present invention relates to a method and an apparatus for biological purification of wastewater with no excess activated sludge by subjecting a mechanically and/or chemically pretreated wastewater to the conditions of total endogenous respiration at aeration with one or more surface turbine type aerators of 5.10⁻² to 12.10⁻² kW/m³ of wastewater, at a microorganism to food ratio of 20 to 100. The height of the liquid level in the basin is at least 5 m. There is provided a high-grade effluent at low capital and operational investment.
    公开号:SU1729289A3
    申请号:SU874203948
    申请日:1987-12-24
    公开日:1992-04-23
    发明作者:Николич Огниен；Краль-Баретич Ядранка；Кошчина-Корунич Смиляна
    申请人:Ина Рафинерия Нафте Риека Н.Сол.О.Ооур Производня Горива И Аромата За Н.Суб.О Друге Радне Организацийе (Фирма)；
    IPC主号:
    专利说明:

    (L
    WITH
    The invention relates to the treatment of water and can be used in the biochemical treatment of domestic and industrial wastewater, in particular, chemical and oil refineries.
    The aim of the invention is to reduce the amount of sludge produced while ensuring a high degree of purification.
    The basis of the known methods of biological wastewater treatment is the transformation of dissolved organic and / or inorganic substances (substrates) into the form of activated sludge, which must be removed from the system.
    At the same time, the consumption of a substrate dissolved in wastewater by microorganisms proceeds according to three main schemes:
    energy costs: substrate + 02 - SOA + NAO;
    synthesis of biomass: substrate + MNZ; Ј biomass;
    endogenous respiration :.
    biomass + Oa C02 + MNZ + NaO.
    These processes are in chemical equilibrium. The predominance of one of them is determined by the empirically established M / F ratio, where M is the amount of biomass;
    F is the amount of substrate in the system.
    The value of the ratio M / F is determined by the formula
     and 1T-Xv, 3 V
    M / F
    where Xv, a is the concentration of suspended substances, mg / l;
    v - volume of water to be purified, m;
    So - BPCD of incoming water for treatment, mg / l;
    Q - water consumption, m3 / day.
    Xi
    hO
    h y
    00
    about

    with
    For various biochemical purification processes, the M / F is from 1 to 50.
    The interval 0-1 is characteristic for short-term (high-performance) aeration, 1-5 for normal aeration with or without denitrification, 5-20 for prolonged aeration, 20-100 for sedimentation.
    Wastewater treatment in a settling tank at M / F 20 is characterized in that the sludge of activated sludge is acquired, the ability to disperse and in fact are suspended. At the same time, the amount of oxygen used for energy costs is the smallest compared with other methods of biochemical purification.
    The choice of the type of aerators and their required amount is made on the basis of the empirical indicator of the EFC, which is the ratio between the amount of oxygen supplied from the aerator to the flakes of active sludge to the total amount of oxygen supplied. The magnitude of the ERC depends on the type of biological reservoir and its design, the type of aerator, the ratio of aerator's capacity to the volume of the biological reservoir, the quality characteristics of the water being purified (temperature, size of MIC, biomass concentration).
    Table 1 presents the dependence of the degree of retention of activated sludge under conditions of complete mixing on the magnitude of the EPC for various types of aerators.
    Thus, wastewater aeration is carried out so that energy consumption is minimal, active sludge is suspended, and the EPC value is kept as high as possible.
    The choice of parameters is due to the following.
    In order to achieve a high degree of purification and to ensure the conditions of complete endogenous respiration, in which no excess sludge is formed, the value of the ratio M / F 20-100 is necessary.
    This interval is maintained for a minimum reservoir depth by a turbine-type surface aerator of 5-10 kW / m, for a maximum of 12-10 kW / m. The minimum depth of the biological reservoir is 5 m, the maximum is determined by the possibility of carrying out the process of biological treatment.
    For carrying out the process, wastewater after preliminary mechanical and chemical treatment is fed to a biological tank 1 equipped with one or several aerators 2 mixing the contents of the tank, after which the pipeline 3 supplies them to a septic tank 4,
    from where the waste stream is diverted via pipeline 5, and the excess sludge is fed to pipeline 6, and the excess sludge is either recycled through pipeline 7 to tank 1 or removed via pipeline 8.
    The waste stream through conduit 5 and the excess sludge recirculating through conduit 8 is fed to biological reservoir 9 with a distance of at least 5 meters from the bottom of the reservoir to the surface of the wastewater.
    The tank 9 is equipped with one or several surface aerators 10 turbine type with a capacity of 5-10 2-12-10 2 kW / m of waste water, which are pressed
    activated sludge to the bottom of tank 9 and slow down its ascent. The waste stream is cleared from the sludge via pipeline 11 and fed to a biofilter 12. Purified water is discharged through pipeline 13.
    Part of the sediment after filtering excess activated sludge through pipelines 14 and 15 is recycled to biofilter 12. Another part of sediment and excess activated sludge is fed through pipelines 14 and 16 to biological tank 9. Depth of biological tank 9 should be at least 5 m, while the cross-sectional shape can be arbitrary (round, square, rectangular, etc), so that
    Tank design can be optimized with minimal volume.
    PRI me R 1. Purify the wastewater of an oil refinery and carry it out only in a biological
    reservoir 9. The height of the liquid level in the biological reservoir is 6 m. The power of aerators of the turbine type is -6.75 kW / m. The M / F ratio in the biological reservoir is 25-30, the capacity
    reservoir - 6 thousand m3.
    Table 2 presents the characteristics of the refinery wastewater before and after treatment.
    The data of Table 2 indicate that the high purification efficiency in the proposed method is achieved at high pH values of the source water and significant fluctuations in the concentrations of contaminated components. In the case of salvo emissions, when all microorganisms in the biological reservoir die, the activated pulp is regenerated for 24 hours, while according to a known method, it takes 15-25 days for regeneration. Besides
    this in the proposed method there is no formation of excess sludge.
    PRI mme R 2. Purification in full is subjected to waste water generated during gasification and coking of coal, characterized by high COD, VPK and VOC, as well as a significant content of nitrogen compounds.
    The cleaning is carried out in a biological tank with a depth of 7 m, a volume of 11 thousand m3. The liquid level in the tank is 6 m, the power of the turbine-type surface aerator is kW / m3 of wastewater, the M / F ratio is 40. Due to the high ammonia content in the wastewater after the biological tank 9, they are fed to the biofilter 12. Excess sludge is recycled from the biofilter to biological reservoir, where it is in conditions of complete endogenous respiration.
    Table 3 presents data on the efficiency of water purification from gasification and coking of coal. No excess sludge is generated during processing.
    PRI me R 3. Household waste water with high BOD and suspended solids is subjected to purification.
    The purification is carried out in a biological reservoir 9 under the conditions of Example 1. The purified wastewater has a BL (5–20 mg / l and contains 10 mg / l suspended solids.
    Compared with the known method, according to which the waste water is subjected to mechanical treatment to remove suspended solids, flocculant treatment, removal of the formed sludge, subsequent thickening and processing, in the proposed method the excess sludge
    Aerator Type
    Turbine type diffusion surface agitator
    Propeller-type Surface Mixer Turbine-type Submersible Mixer
    0
    five
    0
    five
    0
    50
    not formed, which significantly reduces capital and operating costs.
    Table 4 presents data on the number of sludge produced in various types of biological treatment.
    The use of the proposed method allows, while ensuring a high degree of wastewater treatment, to reduce the amount of sludge produced and increase the efficiency of the cleaning process.
    权利要求:
    Claims (2)
    [1]
    1. A method of biochemical wastewater treatment, including preliminary mechanical and / or chemical treatment of water, aeration in the presence of activated sludge, followed by separation of purified water and the resulting sludge, characterized in that, in order to reduce the amount of sludge produced while ensuring a high degree of purification, aeration carried out by one or several turbine-type surface aerators with a capacity of 5 10 2-12 "10 2 kW / m 3 of water in a tank at least 5 m deep under conditions of complete endogenous respiration, while observing Ichin biomass ratio to the substrate of 20 to 100.
    [2]
    2. A method according to claim 1, characterized in that the ratio of biomass to substrate is determined by the formula
    where M is the amount of biomass,
    F — amount of substrate, m3 / day mg / l;
    Hu, and the amount of suspended substances in the tank, mg / l;
    v is the volume of treated water, m3;
    So BOD & incoming water for treatment, mg / l; Q - water consumption, m3 / day.
    Table
    ERC Parameter
    Retention of activated sludge under conditions of complete mixing

    Good (regardless of depth) 0.3–5 m is good; 5 m is bad
    1-6 m good
    Good regardless of depth
    Note: TOC - total organic carbon
    Table 2
    T a b l and c a 3
    Table4
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    同族专利:
    公开号 | 公开日
    EP0275538A2|1988-07-27|
    ES2044911T3|1994-01-16|
    DE3787006D1|1993-09-16|
    US5186837A|1993-02-16|
    DE3787006T2|1993-12-16|
    YU224086A|1989-06-30|
    AT92898T|1993-08-15|
    EP0275538B1|1993-08-11|
    EP0275538A3|1988-08-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3980556A|1974-01-25|1976-09-14|Ontario Research Foundation|Adsorption biooxidation treatment of waste waters to remove contaminants therefrom|
    CH572003A5|1974-11-18|1976-01-30|Kaelin J R|
    US4643830A|1977-11-04|1987-02-17|Reid John H|Process for operating a total barrier oxidation ditch|
    US4537682A|1982-01-29|1985-08-27|Environmental Research & Technology|Activated sludge wastewater treating process|US5958241A|1995-08-22|1999-09-28|The Louisiana Land & Exploration Co.|Waste treatment and minimization system|
    US6555002B2|2000-10-06|2003-04-29|Premier Wastwater International, Llc|Apparatus and method for wastewater treatment with enhanced solids reduction |
    US6391203B1|2000-11-22|2002-05-21|Alexander G. Fassbender|Enhanced biogas production from nitrogen bearing feed stocks|
    US7005069B2|2004-04-27|2006-02-28|Passaic Valley Sewerage Commissioners|Apparatus and method for aeration of wastewater|
    GB0518508D0|2005-09-10|2005-10-19|Christian Stuart J|Treatment of waste|
    CN102574715B|2009-08-28|2014-11-26|关西热化学株式会社|Biotreatment method|
    US10927014B1|2018-06-06|2021-02-23|Raymond C. Sherry|Waste water treatment to reduce BOD/COD|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    YU224086A|YU224086A|1986-12-24|1986-12-24|Device for biological purifying of waste waters without remainings of active sludge|
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