• 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 invention relates to a bioreactor having a tank (1) containing at least one bioreactor compartment (1a-1c) having a carrier on which a biofilm can grow, feed means for supplying water to be purified to the bioreactor compartment (1a-1c), a first longitudinal end (1a-1c) at one opposite longitudinal end for removing processed water from the compartment (1a-1c), means (7) for supplying the reaction gas required for the purification process to the bioreactor compartment, and means for rotating the carrier and water to be purified within the compartment. The bioreactor compartment (1a-1c) is provided with a perforated tube (4) extending in its longitudinal direction, spaced from the interior walls (8, 9) of the bioreactor compartment, with control means (2a-2c, 13a-13c) in the inlet end region 4) an external bioreactor space, from which purified water is drained into and out of the perforated tube (4) through an outlet at the outlet end of the bioreactor compartment (1a-1c).
    公开号:FI20175367A1
    申请号:FI20175367
    申请日:2017-04-24
    公开日:2018-10-25
    发明作者:Martti Naukkarinen；Pasi Korvonen
    申请人:Clewer Aquaculture Oy；
    IPC主号:
    专利说明:

    The present invention relates to a bioreactor having a reservoir containing at least one bioreactor compartment having a carrier on which the biofilm can grow, feed means for supplying water to be purified to the bioreactor compartment at a first longitudinal end of the compartment, and means for circulating the water to be purified within the compartment.
    In the biological purification of water, such as waste water, the water is passed through a reactor which utilizes microorganisms to convert the impurities in the water into harmless end products such as carbon dioxide, minerals and water. Microorganisms are grown, for example, on carriers on which microorganisms can grow as biofilms. In biological water purification, microorganisms can also bind non-biodegradable products such as heavy metals to biomass. Purification can be done aerobically or anaerobically.
    It is an object of the present invention to provide a bioreactor which is particularly suitable for treating circulating fish farming water by nitrification and denitrification. The purpose is to remove ammonium and nitrogen compounds from the water with the help of biologically compatible bacteria so that water is a good habitat for fish. Water-purifying bacteria form colonies on the surfaces of the carrier elements. The solution of the invention can also be used in other water purification processes, such as wastewater treatment.
    To achieve the object of the invention, the bioreactor according to the invention is characterized in that the bioreactor compartment is provided with a longitudinally routed tube 30 spaced from the interior walls of the bioreactor compartment and having inlet end thence through an outlet at the outlet end of the bioreactor compartment.
    20175367 prh 24-04-2017
    Some preferred embodiments of the invention are described in the dependent claims.
    The bioreactor according to the invention consists of a tank inside the tank and the carrier material formed by the carrier bodies therein, as well as various parts for controlling the flow of water and keeping the carrier bodies away from the flow. The operation also includes aeration, which moves the carrier bodies and also provides oxygen to the process for nitrification.
    The invention will now be further described with reference to the accompanying drawings, in which:
    Figure 1 shows a bioreactor according to the invention in end elevational view; Fig. 5 is a cross-sectional view of the compartment of Fig. 4, showing a bioreactor according to the invention, one compartment of which is provided for a denitrification process;
    The embodiment shown in the figures includes a container 1 of rectangular cross-section with a bottom part 8, side walls 9 and end walls defining a basin 30 therebetween. Preferably, the pool is covered by a cover portion 10. At least one bioreactor compartment is formed in the basin having carrier bodies (not shown) on which the biofilm can grow. Guide plates 5 extending longitudinally (perpendicular to the plane of the paper) extending from the side walls 9 in an oblique inward and upward direction to the lid portion 10 are provided in the region of the upper portion of the bioreactor compartment.
    20175367 prh 24-04-2017 The baffles 5 facilitate the circulation of the water inside the compartment, for example, when the flow of air protruding from the air pipes 7 acts as the driving force of the rotational motion. At the top of the container is an air space 6, in which the gases in the water can rise and leave, e.g.
    A pipe 4 is installed through the basin with its opening and end open at the pool wall or outside the basin. The tube 4 is perforated, either partially or completely. At the start end, where the water to be purified exits from the inside of the pipe, the aperture 10 is preferably at least 50% of the peripheral area of the pipe. The perforation is dimensioned to prevent the carrier bodies from moving inside the tube. Dams are allowed at this point to distribute the water flow more evenly into the basin. The pipe diameter is selected for various purposes. Inside the pipe 4, there may be another intact pipe (not shown) for controlling the flows. A barrier plate 13a-13c is provided on the inner side of the tube 4 at a position in the front of which it is desired that water flow from the inside of the tube through the perforations to the outside of the tube. The purpose is to cause the water to be treated to flow as evenly as possible throughout the mass of the carrier, thereby maximizing the biological activity capacity. At the shut-off plate 13a-13c outside the tube 20, there is a baffle baffle 2a-2c which forces water to flow through the reactor cross-section as seen through the flow opening 14 between the outer edges of the baffle 2a-2c and the tank sides 8, 9.
    Figures 2 and 3 show a two- and three-compartment bioreactor, respectively, in which the pool is divided by partitions 3a, 3b through which the tube 4 extends, so that the reactor compartments follow the same sequentially and quantitatively as desired. The perforated tube 4 preferably extends along the entire length of the container between the end walls 11 and 12 of the container 1. Between the barrier plate 13a inside the pipe 4 and the first partition 3a, water flows back into the pipe 4 through the pipe holes and continues forward to the other side of the wall 3a where the same flow pattern is repeated as the baffle 2b guides the water flow around the pipe 4. The same is repeated after the next wall 3b in the embodiment shown in Figure 3 with three offices
    20175367 prh 24-04-2017 Actor Department. The shut-off plate 13a-13c may also have an opening or be turned so that some or all of the flow passes through the reactor compartment.
    The basin is designed to fill as much carrier as possible, giving more power per bottom area. The carrier bodies form a bed which is rotated by aeration so that the bed circulates around the routed tube 4 or else the water mixes well. The aeration pipes 7 are placed at a depth of up to about 1.5 meters from the water surface and the air is blown to achieve the desired movement of the carrier bed. Blowing too deep can cause harmful nitrogen10 gas over-saturation. Rotation can be promoted, for example, by means of baffles 5 which are mounted at an angle of 45 degrees and are disposed in the flow direction so that the imaginary circle of rotation is flush with the top of the bed or otherwise facilitates operation. The air pipes 7 are placed on the side of the basin near the outer wall 9 so that the air coming from them lifts the carrier bed upwards from one side of the bed if it is desired to rotate the carrier bed. In a circulating fish farm, using a nitrification (including denitrification) process, the water is aerated to allow the carbon dioxide to be blown out of the water. In this sense, the use of air here does not increase the necessary costs. By allowing most of the flow to pass by a compartment and using this periodically or continuously as denitrification, the water thus treated can again be passed through the subsequent compartment to nitrification, thus avoiding the sudden damage of the packing reactor.
    Open-source bioreactors are used by various operators and conventional bioreactors, for example, in the case of a moving bed reactor, often have only a carrier bed of about 80 cm. The solutions provided by these methods bring a significant increase in capacity.
    In Denmark and Central Europe, for example, there are long-standing shallow tanks where this method could easily be placed in ponds and directly increased their capacity. The solution according to the invention is particularly suitable for renovation sites. In terms of construction costs, the solution according to the invention is inexpensive and, for example, installation in open basins is quick. Using an open pool has its own benefit in the event of a disturbance compared to a closed tank, as it can
    20175367 prh 24-04-2017 ta easier location of the potential interference. The pool is most often covered to prevent unwanted algae and bacteria from being exposed to sunlight.
    The routed pipe used in the solution of the invention is preferably steel.
    In the denitrification step, the water to be purified can be mixed and spun with or without nitrogen.
    Figures 4 and 5 illustrate, by way of example, one embodiment for accelerated initiation of the denitrification process. In this exemplary embodiment, the central compartment Ib of the three-compartment bioreactor is closed by a lid 10 provided with a gas outlet 15 for discharging gasses from the water to be purified. The outlet 15 is connected to a blower 16 which feeds the reaction gas through the conduit 17 through the aeration conduits 7 to the bioreactor compartment. The bioreactor is typically fed with air as a reaction gas for use in an aerobic process. The anaerobic for denitrification, in which the nitrate nitrogen is reduced to nitrogen gas (NO3 _ - "NO 2" -> NO -> N 2 O -> N 2), air can be circulated by means of fan 16 in a closed loop, whereby the oxygen from the air dissolves cleaned air bubbles in water and the bacteria on the surface of the carrier bodies consume such oxygen dissolved in water. As a result, the recirculated air gradually becomes deoxygenated, mainly containing nitrogen gas, which is generated during the denitrification process. This recycled gas, essentially composed of nitrogen gas, allows the carrier to remain in continuous motion. Instead of the recycled reaction gas, another non-oxygen gas can be used to keep the carrier in motion. Keeping the carrier bed in motion continuously causes the water to be treated to be evenly distributed throughout the carrier area and thus to provide a better processing power and maintain the carrier clean. The bioreactor compartment cover 10 is provided with a breather 18 to balance pressure inside and outside the bioreactor compartment. The water to be purified is passed continuously or heavily through the compartment used for denitrification at the desired flow rate.
    If necessary, oxygen-containing gas may sometimes be blown into the compartment to prevent the formation of hydrogen sulphide. Other sections la and le may be open or covered.
    The solution according to the invention can also be applied, e.g. around the center of rotation.
    Reference number list container
    20175367 prh 24-04-2017
    2a-2c
    3a-3b
    8
    13a-13c
    18 flow baffle divider baffle routed tube baffle tank top air pipes tank bottom tank sidewall tank cover tank first end tank second end stopper flow port gas outlet fan reaction gas inlet breather
    权利要求:
    Claims (8)
    [1]
    A bioreactor having a reservoir (1) containing at least one bioreactor compartment (1a-1c) having a feed material on which a biofilm can grow,
    5 for supplying distilled water to the bioreactor compartment (la-lc) from a first longitudinal end of the compartment, discharge means at one of the opposite longitudinal ends of the compartment (la-lc) for removing processed water from the compartment (la-lc), means for supplying to circulate the water to be purified
    10 inside the compartment, characterized in that a longitudinally routed tube (4) is provided in the bioreactor compartment (1a-1c), which is spaced from the internal walls (8, 9) of the bioreactor compartment and has control elements (2a-2c, 13a) 13c) for directing the water to be purified to the external bioreactor space of the pipe (4), from which the purified water is discharged inside and out of the perforated pipe (4) through an outlet at the outlet end of the bioreactor compartment (1a-1c).
    [2]
    Bioreactor according to claim 1, characterized in that at least two bioreactor compartments (1a-1c) are arranged in the tank (1), which are separated by a partition (3a-3b).
    [3]
    Bioreactor according to Claim 1 or 2, characterized in that the tank (1) has a rectangular cross-section and has a bottom (8), side walls (9) and a lid (10) having longitudinally extending tanks in the upper region of the tank (1). guide plates (5) which facilitate the presence of the bioreactor compartment (2a-2c)
    25 in rotating the carrier and water.
    [4]
    Bioreactor according to one of the preceding claims, characterized in that the control elements (2a-2c, 13a-13c) comprise an inner barrier plate (13a13c) of the tube (4) and an external baffle plate (2a-2c) extending from the outer surface of the tube (4).
    30 pins forming a flow opening spaced from the interior walls (8, 9) of the bioreactor compartment.
    [5]
    Bioreactor according to Claim 4, characterized in that the shut-off plate (13a-13c) is formed as a valve means by which the water to be purified can be directed, if necessary, inside the perforated tube (4) bypassing the desired bioreactor compartment.
    [6]
    Bioreactor according to one of the preceding claims, characterized in that
    The material of the 5 perforated tubes (4) is steel.
    [7]
    Bioreactor according to any one of the preceding claims, characterized in that at least one compartment (Ib) is provided with a lid (10) and means (15-17) for circulating the reaction gas in the compartment in a closed circuit to provide denitrification.
    [8]
    10 pouring process in the compartment.
    类似技术:
    公开号 | 公开日 | 专利标题
    JP6810038B2|2021-01-06|Water treatment modules, reactors, systems and water treatment methods
    FI127756B|2019-02-15|Bioreactor
    JP4440826B2|2010-03-24|Membrane separation oxidation ditch
    JP2014113511A|2014-06-26|Membrane separation apparatus, and operation method of membrane separation apparatus
    JP4409532B2|2010-02-03|Apparatus for treating wastewater containing high-concentration nitrogen such as livestock wastewater and manure, and its treatment method
    JP2008221162A|2008-09-25|Denitrifying treatment tank and denitrifying treatment method
    JP5992807B2|2016-09-14|Waste water treatment apparatus and waste water treatment method
    JP2009261994A|2009-11-12|Treatment method and treatment apparatus of drainage
    KR20190108327A|2019-09-24|Carrier assembly for denitrification and anoxic tank provided with the same
    JP7016622B2|2022-02-07|Membrane separation activated sludge treatment equipment and membrane separation activated sludge treatment method
    KR101303820B1|2013-09-04|Water treatmen apparatus for removing nitrogen and phosphorus using upflow and downflow complete mixing chain reaction
    JP4938582B2|2012-05-23|Reaction tank for sewage treatment
    JP2019076887A|2019-05-23|Waste water treatment apparatus and waste water treatment method
    JP7016623B2|2022-02-07|Membrane separation activated sludge treatment equipment and membrane separation activated sludge treatment method
    JP2018187539A|2018-11-29|Membrane separation active sludge treatment device, and membrane separation active sludge treatment method
    JP6931551B2|2021-09-08|Membrane separation activated sludge treatment equipment and membrane separation activated sludge treatment method
    JP2009154144A|2009-07-16|Gas-liquid mixer and gas-liquid mixing method
    WO2021131485A1|2021-07-01|Microorganism reaction tank
    TWI567029B|2017-01-21|Wastewater treatment tank
    JP2002320994A|2002-11-05|Method for operating oxidation ditch
    JP2019034295A|2019-03-07|Water treatment system
    JP2018187540A|2018-11-29|Membrane separation active sludge treatment device, and membrane separation active sludge treatment method
    KR100914690B1|2009-08-28|Microbe reactor
    KR200367958Y1|2004-11-16|Biofiltering Apparatus for Sewage and Wastewater Treatment System
    KR20000011755U|2000-07-05|Air separation / removal in feed water and feed water mixing device
    同族专利:
    公开号 | 公开日
    HRP20210550T1|2021-05-28|
    FI127756B|2019-02-15|
    RS61707B1|2021-05-31|
    WO2018197744A1|2018-11-01|
    AU2018259114A1|2019-10-31|
    RU2019133776A|2021-05-25|
    EP3615478A1|2020-03-04|
    US10961140B2|2021-03-30|
    CL2019003042A1|2020-03-27|
    RU2019133776A3|2021-05-25|
    US20200048120A1|2020-02-13|
    PT3615478T|2021-04-09|
    RU2754566C2|2021-09-03|
    ES2863981T3|2021-10-13|
    PL3615478T3|2021-08-02|
    SI3615478T1|2021-07-30|
    KR20190139877A|2019-12-18|
    LT3615478T|2021-04-26|
    CA3060032A1|2018-11-01|
    HUE055147T2|2021-11-29|
    DK3615478T3|2021-04-12|
    MX2019012607A|2020-02-05|
    CN110891906A|2020-03-17|
    EP3615478B1|2021-03-10|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    SU71293A1|1945-05-03|1947-11-30|И.П. Калитов|Liquid mixing apparatus|
    US2740616A|1952-11-03|1956-04-03|Willie W Walden|Mixer|
    GB912433A|1960-09-27|1962-12-05|Hartleys Stoke On Trent Ltd|Improvements in gas circulation relating to sludge digestion tanks for the treatmentof sewage and industrial effluents|
    SU1105476A1|1983-06-24|1984-07-30|Томский инженерно-строительный институт|Device for aeration of liquid|
    DE3506687A1|1985-02-26|1986-08-28|Linde Ag, 6200 Wiesbaden|METHOD AND DEVICE FOR BIOLOGICAL WASTE WATER TREATMENT|
    DE69104629D1|1990-01-23|1994-11-17|Kaldnes Miljoteknologi As|METHOD AND REACTOR FOR PURIFYING WATER.|
    DE4009180A1|1990-03-22|1991-09-26|Bayer Ag|DEVICE FOR SOLID RETURN TRANSPORT IN LONG-FLOWED FLUIDED BED REACTORS FOR WASTE WATER TREATMENT WITH CARRIER PARTICLES|
    US6015490A|1995-05-23|2000-01-18|Ebara Corporation|Carrier-separating and water-collecting mechanism of wastewater treatment equipment|
    JPH10304789A|1997-03-05|1998-11-17|Masuo Maruyama|Bottom sand for culturing fish and shells, fish and shells culturing/rearing pipe using this and culturing device connecting many of the pipes|
    EP1131266A4|1998-09-28|2004-05-12|Glen D Lindbo|Wastewater treatment tank with influent gates and pre-react zone with an outwardly flared lower portion|
    WO2001004060A2|1999-07-12|2001-01-18|Oy Clewer Ltd|Method of purifying water, suitable bacteria for the method and use thereof|
    FI20065006A0|2006-01-04|2006-01-04|Brandco Ab Oy|Bioreactor and Method for Biological Purification of Water in a Bioreactor|
    ES2410164T3|2006-01-04|2013-07-01|Clewer Oy|Bioreactor and method for biological purification of water.|
    KR100862184B1|2007-03-28|2008-10-09|포항공과대학교 산학협력단|Anaerobic or anoxic reactor employing density-controlled medias, apparatus and method for treating wastewater using the same|
    CN201154929Y|2007-12-04|2008-11-26|北京工业大学|Sewage biological denitrification and sludge decrement coupling biological reaction device|
    AT509427B1|2010-01-28|2016-10-15|Ingerle Kurt|PROCESS AND DEVICE FOR BIOLOGICAL WASTE CLEANING|
    FI20116093A|2011-11-04|2013-05-05|Clewer Oy|Water treatment plant|
    AU2012344378A1|2011-12-02|2014-07-24|Inter Aqua Advance A/S|Biological treatment tank or tank series with air-lift and biocarriers|
    RU2505487C2|2011-12-19|2014-01-27|Закрытое акционерное общество "Высокоэффективные электрозарядные технологии и оборудование" |Multisectional contact reservoir for water processing with ozone|
    WO2013133443A1|2012-03-09|2013-09-12|メタウォーター株式会社|Wastewater treatment device, wastewater treatment method, wastewater treatment system, control device, control method, and program|
    US8871094B2|2012-07-30|2014-10-28|R N Industries, Inc.|Wastewater treatment facility and bioreactor for treating wastewater from oil and gas exploration and production|
    CN205527968U|2016-01-27|2016-08-31|北京中电加美环保科技有限公司|Biological fluidized bed|NO20191322A1|2019-11-06|2021-05-07|Sterner As|Device for biological treatment of water for Aquaculture facilities|
    RU208009U1|2021-09-28|2021-11-29|Федеральное государственное бюджетное образовательное учреждение высшего образования "Саратовский государственный аграрный университет имени Н.И. Вавилова"|Biofilter for water purification in fish culture systems|
    法律状态:
    2019-02-15| FG| Patent granted|Ref document number: 127756 Country of ref document: FI Kind code of ref document: B |
    优先权:
    申请号 | 申请日 | 专利标题
    FI20175367A|FI127756B|2017-04-24|2017-04-24|Bioreactor|FI20175367A| FI127756B|2017-04-24|2017-04-24|Bioreactor|
    KR1020197030687A| KR20190139877A|2017-04-24|2018-04-10|Bioreactor with Mobile Carrier|
    SI201830256T| SI3615478T1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    HUE18727340A| HUE055147T2|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    ES18727340T| ES2863981T3|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    PL18727340T| PL3615478T3|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    RU2019133776A| RU2754566C2|2017-04-24|2018-04-10|Bioreactor for water purification|
    CA3060032A| CA3060032A1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    PT187273404T| PT3615478T|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    DK18727340.4T| DK3615478T3|2017-04-24|2018-04-10|BIOREACTOR WITH MOVING CARRIERS|
    AU2018259114A| AU2018259114A1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    PCT/FI2018/050256| WO2018197744A1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    LTEP18727340.4T| LT3615478T|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    EP18727340.4A| EP3615478B1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    RS20210418A| RS61707B1|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    US16/606,824| US10961140B2|2017-04-24|2018-04-10|Bioreactor with moving carriers|
    CN201880026132.8A| CN110891906A|2017-04-24|2018-04-10|Bioreactor|
    MX2019012607A| MX2019012607A|2017-04-24|2018-04-10|Bioreactor with moving carriers.|
    CL2019003042A| CL2019003042A1|2017-04-24|2019-10-23|Bioreactor with mobile carriers.|
    HRP20210550TT| HRP20210550T1|2017-04-24|2021-04-07|Bioreactor with moving carriers|
    [返回顶部]