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公开(公告)号:US08066878B2
公开(公告)日:2011-11-29
申请号:US11919410
申请日:2005-06-10
申请人: Sjoerd Hubertus Josef Vellinga , Jelle Hendrik de Boer , Antonius Johannes Jorna , Leonard Hubertus Alphonsus Habets
发明人: Sjoerd Hubertus Josef Vellinga , Jelle Hendrik de Boer , Antonius Johannes Jorna , Leonard Hubertus Alphonsus Habets
IPC分类号: C02F3/28
CPC分类号: C12M21/04 , C02F3/2846 , C02F3/2873 , C02F2209/03 , C12M23/36 , C12M29/18
摘要: The invention relates to an anaerobic purification device for purification of influent. The device has a reactor tank, an inlet for introducing influent into the tank, a water collecting device for collecting purified water, a gas collecting system for collecting gas from the fluid contained in the reactor, a gas-liquid separation device, a riser for passing liquid into the separation device by gas lifting action caused by gas collected in the gas collecting system, and a downer for returning liquid and sludge from the separation device into the lower tank section. According to the invention this device is characterized in that it is arranged to define, in the downer at the level of the liquid surface, a head pressure of, at least, approximately 1.4 m water column (approximately 0.14 bar). The invention also relates to a method for anaerobic purification device for purification of influent.
摘要翻译: 本发明涉及一种用于净化流入物的厌氧净化装置。 该装置具有反应槽,用于引入流入槽的入口,用于收集净化水的集水装置,用于从包含在反应器中的流体收集气体的气体收集系统,气液分离装置,用于 通过气体收集系统中收集的气体引起的气举动作将液体送入分离装置,以及用于将液体和污泥从分离装置返回到下部罐部分的下降器。 根据本发明,该装置的特征在于,其布置成在液面的液面处在下降器中限定至少约1.4m水柱(大约0.14巴)的头部压力。 本发明还涉及用于净化流入物的厌氧净化装置的方法。
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公开(公告)号:US20090308806A1
公开(公告)日:2009-12-17
申请号:US11919410
申请日:2005-06-10
申请人: Sjoerd Hubertus Jozef Vellinga , Jelle Hendrik De Boer , Antonius Johannes Jorna , Leonard Hubertus Alphonsus Habets
发明人: Sjoerd Hubertus Jozef Vellinga , Jelle Hendrik De Boer , Antonius Johannes Jorna , Leonard Hubertus Alphonsus Habets
IPC分类号: C02F3/28
CPC分类号: C12M21/04 , C02F3/2846 , C02F3/2873 , C02F2209/03 , C12M23/36 , C12M29/18
摘要: The invention relates to an anaerobic purification device for purification of influent. The device has a reactor tank, an inlet for introducing influent into the tank, a water collecting device for collecting purified water, a gas collecting system for collecting gas from the fluid contained in the reactor, a gas-liquid separation device, a riser for passing liquid into the separation device by gas lifting action caused by gas collected in the gas collecting system, and a downer for returning liquid and sludge from the separation device into the lower tank section. According to the invention this device is characterized in that it is arranged to define, in the downer at the level of the liquid surface, a head pressure of, at least, approximately 1.4 m water column (approximately 0.14 bar). The invention also relates to a method for anaerobic purification device for purification of influent.
摘要翻译: 本发明涉及一种用于净化流入物的厌氧净化装置。 该装置具有反应槽,用于引入流入槽的入口,用于收集净化水的集水装置,用于从包含在反应器中的流体收集气体的气体收集系统,气液分离装置,用于 通过气体收集系统中收集的气体引起的气举动作将液体送入分离装置,以及用于将液体和污泥从分离装置返回到下部罐部分的下降器。 根据本发明,该装置的特征在于,其布置成在液面的液面处在下降器中限定至少约1.4m水柱(大约0.14巴)的头部压力。 本发明还涉及用于净化流入物的厌氧净化装置的方法。
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公开(公告)号:US5972219A
公开(公告)日:1999-10-26
申请号:US875077
申请日:1997-07-17
CPC分类号: C02F3/2846 , C02F3/30 , C02F3/301 , C02F3/302
摘要: A process is described for the aerobic treatment of effluent in a reactor of the UASB type, into the bottom of which the effluent to be treated is fed and, at the same time, oxygen is fed in an amount such that the growth of a facultative and an aerobic biomass is promoted. An apparatus for the aerobic treatment of effluent is also described, which apparatus consists of a UASB rector, distributors for supplying liquid and aeration means being located at the bottom of the reactor and means for integrated settling of biomass and gas collection being located at the top of the reactor. The apparatus can also be an integrated anaerobic/aerobic reactor.
摘要翻译: PCT No.PCT / NL96 / 00048 Sec。 371日期1997年7月17日 102(e)日期1997年7月17日PCT 1996年1月31日PCT PCT。 第WO96 / 23735号公报 日期1996年8月8日描述了用于在UASB型反应器中对流出物进行好氧处理的方法,其中将待处理的流出物进料到其底部,并且同时以一定的量进料氧气, 促进兼性和有氧生物质的生长。 还描述了用于污水的需氧处理的装置,该装置包括UASB检验器,用于供应液体的分配器和位于反应器底部的通气装置,以及位于顶部的生物质和气体收集的集成沉降装置 的反应器。 该装置也可以是综合的厌氧/需氧反应器。
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公开(公告)号:US06372139B1
公开(公告)日:2002-04-16
申请号:US09705889
申请日:2000-11-06
IPC分类号: C02F330
CPC分类号: D21C11/0021 , C02F1/001 , C02F1/24 , C02F1/444 , C02F3/02 , C02F3/286 , C02F9/00 , C02F2001/007 , C02F2103/28 , Y02W10/15 , Y10S210/928
摘要: A method for the treatment of process water or effluent from a papermaking process, in which this water is subjected to at least one anaerobic purification step, an aeration step and a solids separation step and the water is then returned to the production process, and at least two treated water streams of different quality, which originate from a different combination of purification steps, are returned to different points in the production process.
摘要翻译: 一种用于处理来自造纸方法的工艺用水或流出物的方法,其中该水经受至少一个厌氧净化步骤,通气步骤和固体分离步骤,然后将水返回到生产过程中,并且在 不同质量的至少两种来自不同净化步骤组合的经过处理的水流在生产过程中返回到不同点。
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公开(公告)号:US6063273A
公开(公告)日:2000-05-16
申请号:US306413
申请日:1999-05-06
申请人: Leonard Hubertus Alphonsus Habets , Antonius Johannes Hendrikus Hyacinthus Engelaar , Sjoerd Hubertus Jozef Vellinga
发明人: Leonard Hubertus Alphonsus Habets , Antonius Johannes Hendrikus Hyacinthus Engelaar , Sjoerd Hubertus Jozef Vellinga
CPC分类号: C02F3/2846 , C02F1/24 , C02F3/12 , C02F3/20 , C02F3/30 , C02F3/301 , Y02E50/343 , Y02W10/15
摘要: For the biological purification of waste water, use is made of a column containing a UASB reactor (1) at the bottom and an aerobic reactor (2) at the top. The two reactors (1; 2) are separated from one another by a partition (12) in which openings are provided to allow the anaerobic effluent through into the aerobic reactor. The partition (12) is situated at some distance above the gas collection means (8) in order to form a buffer zone (13) for anaerobic sludge which has flowed through. Preferably, a floatation apparatus (3) is mounted on the aerobic reactor in order to separate biomass from the purified water.
摘要翻译: 对于废水的生物净化,使用在底部含有UASB反应器(1)的塔和位于顶部的需氧反应器(2)。 两个反应器(1; 2)通过隔板(12)彼此分开,在隔板(12)中提供开口以使厌氧流出物进入需氧反应器。 隔板(12)位于气体收集装置(8)上方一定距离处,以形成已经流过的厌氧污泥的缓冲区(13)。 优选地,漂浮装置(3)安装在需氧反应器上以便将生物质与净化水分离。
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