公开(公告)号：US20130140246A1

公开(公告)日：2013-06-06

申请号：US13687058

申请日：2012-11-28

申请人： Malcolm Fabiyi

发明人： Malcolm Fabiyi

IPC分类号： C02F1/72

CPC分类号： B01F3/04262 ,  B01F3/04106 ,  B01F3/04248 ,  B01F3/04439 ,  B01F3/04539 ,  B01F3/04609 ,  B01F7/00416 ,  B01F7/00733 ,  B01F7/22 ,  B01F13/0049 ,  B01F2003/04319 ,  B01F2003/04326 ,  B01F2003/0439 ,  B01F2003/0456 ,  B01F2003/04645 ,  B01F2003/04652 ,  B01F2003/04666 ,  B01F2003/04673 ,  B01F2003/0468 ,  B01F2003/04709 ,  B01F2003/04879 ,  C02F1/727 ,  C02F1/74 ,  C02F3/02 ,  C02F3/1284 ,  C02F3/16 ,  C02F3/206 ,  C02F3/26 ,  C02F2101/301 ,  C02F2301/043 ,  C02F2301/046 ,  Y02W10/15

摘要： A means for obtaining high mass transfer efficiencies in surfactant laden wastewater treatment or process systems is disclosed. The present system employs ultrafine bubbles delivered into a high shear region such as in the draft tube or other containment volume of a mechanically agitated contacting system within which an impeller is placed, or in the venturi or divergent-convergent of a pumped loop within which gas-liquid contacting is carried out.

公开(公告)号：US20090050562A1

公开(公告)日：2009-02-26

申请号：US12117791

申请日：2008-05-09

申请人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

发明人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

IPC分类号： C02F3/26

CPC分类号： C02F3/12 ,  B01F3/04609 ,  B01F13/0049 ,  C02F3/16 ,  C02F3/206 ,  C02F3/26 ,  C02F2209/001 ,  C02F2209/10 ,  C02F2209/22 ,  Y02W10/15

摘要： An activated sludge wastewater treatment method is provided. The disclosed method includes: receiving a stream of wastewater into a mixed liquor in an uncovered activated sludge basin; introducing high purity oxygen to the mixed liquor in the activated sludge basin to produce euoxic conditions (i.e. a dissolved oxygen level in the range of between about 5 mg to 15 mg) in the activated sludge basin; passing a portion of the mixed liquor in the activated sludge basin through a clarifier to separate activated sludge and produce an effluent stream and an activated sludge stream; and recycling a portion of the activated sludge stream to the activated sludge basin to produce a mixed liquor having a solids loading of between about 3000 mg and about 10000 mg of suspended solids per liter of mixed liquor and a solids retention time of between about 7 days and 40 days.

摘要翻译： 提供了一种活性污泥废水处理方法。 所公开的方法包括：将废水流接收到未覆盖的活性污泥池中的混合液中; 向活性污泥池中的混合液中引入高纯度的氧气，以产生活性污泥池中的无氧条件（即溶解氧水平在约5mg至15mg之间）; 将活性污泥池中的一部分混合液通过澄清器分离出活性污泥并产生流出物流和活性污泥流; 并将活性污泥流的一部分再循环到活性污泥池中以产生每升混合液体的固体负载量为约3000mg至约10000mg悬浮固体和约7天之间的固体保留时间的混合液 和40天。

公开(公告)号：US20140311972A1

公开(公告)日：2014-10-23

申请号：US14244164

申请日：2014-04-03

申请人： Malcolm Fabiyi ,  Asun Larrea ,  Monica de Gracia

发明人： Malcolm Fabiyi ,  Asun Larrea ,  Monica de Gracia

IPC分类号： C02F3/02

CPC分类号： C02F3/02 ,  C02F3/006 ,  C02F3/301 ,  C02F3/303 ,  C02F11/04 ,  C02F11/121 ,  C02F2209/006 ,  C02F2209/02 ,  C02F2209/04 ,  C02F2209/06 ,  C02F2209/14 ,  C02F2209/15 ,  C02F2209/22

摘要： A method and nitrification system for nitrifying a centrate stream produced from dewatering sludge within a wastewater treatment facility in which the centrate stream into a nitrification reactor containing accumulated centrate with a bacterial population of AOB and NOB nitrifying bacteria to the ammonia content within the centrate stream into nitrates and an oxygen containing gas is introduced into the accumulated centrate to support bacterial activity of the AOB and NOB nitrifying bacteria. Additionally, a conditioning method is obtained in which the bacterial population is grown within the nitrification reactor in conditioning stages that involve the introduction of incoming centrate into the reactor with a successively decreasing degree of dilution.

摘要翻译： 一种用于硝化来自废水处理设备中的脱水污泥产生的中心流的方法和硝化系统，其中所述中心液流进入含有具有细菌群体的AOB和NOB硝化细菌的累积浓度的硝化反应器，以使所述中心流内的氨含量进入 将硝酸盐和含氧气体引入累积的浓度中以支持AOB和NOB硝化细菌的细菌活性。 此外，获得了调节方法，其中细菌群体​​在硝化反应器内在调节阶段生长，其涉及以相继降低的稀释度将进入的中心酸引入反应器。

公开(公告)号：US07699980B2

公开(公告)日：2010-04-20

申请号：US12117785

申请日：2008-05-09

申请人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

发明人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

IPC分类号： C02F3/00

CPC分类号： C02F3/12 ,  B01F3/04609 ,  B01F13/0049 ,  C02F3/16 ,  C02F3/206 ,  C02F3/26 ,  C02F2209/001 ,  C02F2209/10 ,  C02F2209/22 ,  Y02W10/15

摘要： An activated sludge wastewater treatment system is provided. The disclosed system includes: an uncovered activated sludge basin; a high purity oxygen aeration system; a secondary clarifier; a return activated sludge line and a waste activated sludge line; wherein the system operates at a solids loading of between about 3000 mg and about 10000 mg of suspended solids per liter of mixed liquor; a dissolved oxygen level in the aeration basin in the range of between about 5 mg to 15 mg; and a solids retention time of between about 7 days and 40 days.

摘要翻译： 提供了一种活性污泥废水处理系统。 所公开的系统包括：未被覆盖的活性污泥池; 高纯度氧气曝气系统; 次级澄清器 回收活性污泥生产线和废活性污泥生产线; 其中所述系统以每升混合液体约3000mg至约10000mg悬浮固体之间的固体负载运行; 在曝气池中的溶解氧水平在约5mg至15mg之间的范围内; 固体保留时间为约7天至40天。

公开(公告)号：US07699986B2

公开(公告)日：2010-04-20

申请号：US12117791

申请日：2008-05-09

申请人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

发明人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

IPC分类号： C02F3/00

CPC分类号： C02F3/12 ,  B01F3/04609 ,  B01F13/0049 ,  C02F3/16 ,  C02F3/206 ,  C02F3/26 ,  C02F2209/001 ,  C02F2209/10 ,  C02F2209/22 ,  Y02W10/15

摘要： An activated sludge wastewater treatment method is provided. The disclosed method includes: receiving a stream of wastewater into a mixed liquor in an uncovered activated sludge basin; introducing high purity oxygen to the mixed liquor in the activated sludge basin to produce euoxic conditions (i.e. a dissolved oxygen level in the range of between about 5 mg to 15 mg) in the activated sludge basin; passing a portion of the mixed liquor in the activated sludge basin through a clarifier to separate activated sludge and produce an effluent stream and an activated sludge stream; and recycling a portion of the activated sludge stream to the activated sludge basin to produce a mixed liquor having a solids loading of between about 3000 mg and about 10000 mg of suspended solids per liter of mixed liquor and a solids retention time of between about 7 days and 40 days.

摘要翻译： 提供了一种活性污泥废水处理方法。 所公开的方法包括：将废水流接收到未覆盖的活性污泥池中的混合液中; 向活性污泥池中的混合液中引入高纯度的氧气，以产生活性污泥池中的无氧条件（即溶解氧水平在约5mg至15mg之间）; 将活性污泥池中的一部分混合液通过澄清器分离出活性污泥并产生流出物流和活性污泥流; 并将活性污泥流的一部分再循环到活性污泥池中以产生每升混合液体的固体负载量为约3000mg至约10000mg悬浮固体和约7天之间的固体保留时间的混合液 和40天。

公开(公告)号：US20090050552A1

公开(公告)日：2009-02-26

申请号：US12117785

申请日：2008-05-09

申请人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

发明人： Richard A. Novak ,  Malcolm Fabiyi ,  Amitabh Gupta

IPC分类号： C02F3/12

CPC分类号： C02F3/12 ,  B01F3/04609 ,  B01F13/0049 ,  C02F3/16 ,  C02F3/206 ,  C02F3/26 ,  C02F2209/001 ,  C02F2209/10 ,  C02F2209/22 ,  Y02W10/15

摘要： An activated sludge wastewater treatment system is provided. The disclosed system includes: an uncovered activated sludge basin; a high purity oxygen aeration system; a secondary clarifier; a return activated sludge line and a waste activated sludge line; wherein the system operates at a solids loading of between about 3000 mg and about 10000 mg of suspended solids per liter of mixed liquor; a dissolved oxygen level in the aeration basin in the range of between about 5 mg to 15 mg; and a solids retention time of between about 7 days and 40 days.

摘要翻译： 提供了一种活性污泥废水处理系统。 所公开的系统包括：未被覆盖的活性污泥池; 高纯度氧气曝气系统; 次级澄清器 回收活性污泥生产线和废活性污泥生产线; 其中所述系统以每升混合液体约3000mg至约10000mg悬浮固体之间的固体负载运行; 在曝气池中的溶解氧水平在约5mg至15mg之间的范围内; 固体保留时间为约7天至40天。