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公开(公告)号：US07695622B2
公开(公告)日：2010-04-13
申请号：US11930264
申请日：2007-10-31
IPC分类号： C02F3/00
CPC分类号： C02F3/006 , C02F1/78 , C02F3/1221 , C02F3/1273 , C02F11/06 , Y02W10/15
摘要： A system and method for the treatment and reduction of sludge via ozonation in a wastewater treatment process is disclosed. The sludge treatment system comprises: a sludge ozonation reactor coupled to an activated sludge treatment basin and adapted to receive a liquid stream of sludge containing biosolids from the activated sludge treatment basin. The sludge treatment system also includes an ozone-enriched gas injection system operatively coupled to the reactor and adapted to inject ozone-enriched gas into the liquid stream at or upstream of the sludge ozonation reactor. The sludge ozonation reactor is configured to allow effective gas-liquid contacting between the ozone-enriched gas and the liquid stream so as to oxidize the biosolids in the liquid stream and initiate bacterial cell lysis thereby reducing the biosolids. Upon reduction of the biosolids, the liquid stream is returned via a return line to the activated sludge basin or other discharge point.
摘要翻译： 公开了一种在废水处理工艺中通过臭氧处理和还原污泥的系统和方法。 污泥处理系统包括：与活性污泥处理池相连的污泥臭氧化反应器，适于从活性污泥处理池接收含有生物固体的污泥的液体流。 污泥处理系统还包括可操作地耦合到反应器的臭氧富集的气体注入系统，并且适于将臭氧富集的气体注入到污泥臭氧反应器中或上游的液体流中。 污泥臭氧化反应器被配置为允许在富含臭氧的气体和液体流之间有效的气液接触，以便使液体物流中的生物固体氧化，并引发细菌细胞裂解从而减少生物固体。 在还原生物固体后，液流通过返回管线返回到活性污泥池或其他排放点。
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公开(公告)号：US07309432B1
公开(公告)日：2007-12-18
申请号：US11541100
申请日：2006-09-29
IPC分类号： C02F3/00
CPC分类号： C02F3/006 , C02F1/78 , C02F3/1221 , C02F3/1273 , C02F11/06 , Y02W10/15
摘要： A system and method for the treatment and reduction of sludge via ozonation in a wastewater treatment process is disclosed. The sludge treatment system comprises: a sludge ozonation reactor coupled to an activated sludge treatment basin and adapted to receive a liquid stream of sludge containing biosolids from the activated sludge treatment basin. The sludge treatment system also includes an ozone-enriched gas injection system operatively coupled to the reactor and adapted to inject ozone-enriched gas into the liquid stream at or upstream of the sludge ozonation reactor. The sludge ozonation reactor is configured to allow effective gas-liquid contacting between the ozone-enriched gas and the liquid stream so as to oxidize the biosolids in the liquid stream and initiate bacterial cell lysis thereby reducing the biosolids. Upon reduction of the biosolids, the liquid stream is returned via a return line to the activated sludge basin or other discharge point.
摘要翻译： 公开了一种在废水处理工艺中通过臭氧处理和还原污泥的系统和方法。 污泥处理系统包括：与活性污泥处理池相连的污泥臭氧化反应器，适于从活性污泥处理池接收含有生物固体的污泥的液体流。 污泥处理系统还包括可操作地耦合到反应器的臭氧富集的气体注入系统，并且适于将臭氧富集的气体注入到污泥臭氧反应器中或上游的液体流中。 污泥臭氧化反应器被配置为允许在富含臭氧的气体和液体流之间有效的气液接触，以便使液体物流中的生物固体氧化，并引发细菌细胞裂解从而减少生物固体。 在还原生物固体后，液流通过返回管线返回到活性污泥池或其他排放点。
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公开(公告)号：US07497949B2
公开(公告)日：2009-03-03
申请号：US11881845
申请日：2007-07-30
IPC分类号： C02F3/00
CPC分类号： B01F3/04609 , B01F7/00358 , B01F7/0065 , B01F13/0049 , B01F2003/0456 , B01F2003/0468 , C02F3/02 , C02F3/1284 , C02F3/165 , C02F3/206 , Y02W10/15
摘要： A system and method for oxygenating an aerobic sludge digester is provided. The disclosed embodiments include an aerobic sludge digester tank or vessel having a mechanically agitated contactor disposed therein, an oxygen injection subsystem adapted to inject oxygen into the digester tank proximate the mechanically agitated contactor. The embodiments of the mechanically agitated contactor include an agitator or impeller disposed within the draft tube which makes the draft tube the primary site for the gas-liquid mixing. In particular, the agitator or impeller is adapted to create gas bubbles having an average diameter between about 0.3 mm and 3.0 mm which are then dispersed into the aerobic digester. The mass transfer efficiency associated with the present system and method is enhanced from the combined effect of oxygen dissolution into the sludge and greater bubble residence time.
摘要翻译： 本发明提供一种氧气污泥消化器的氧化系统和方法。 所公开的实施例包括一个好氧污泥消化器罐或容器，其中设置有机械搅拌的接触器，氧气注入子系统适于将氧气注入靠近机械搅拌接触器的蒸煮罐中。 机械搅拌的接触器的实施例包括设置在引流管内的搅拌器或叶轮，其使引流管成为用于气液混合的主要部位。 特别地，搅拌器或叶轮适于产生平均直径在约0.3mm至3.0mm之间的气泡，然后将其分散到需氧消化器中。 与现有系统和方法相关的传质效率从氧气溶解到污泥中的联合效应和较大的气泡停留时间得到提高。
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公开(公告)号：US20080128352A1
公开(公告)日：2008-06-05
申请号：US11930264
申请日：2007-10-31
CPC分类号： C02F3/006 , C02F1/78 , C02F3/1221 , C02F3/1273 , C02F11/06 , Y02W10/15
摘要： A system and method for the treatment and reduction of sludge via ozonation in a wastewater treatment process is disclosed. The sludge treatment system comprises: a sludge ozonation reactor coupled to an activated sludge treatment basin and adapted to receive a liquid stream of sludge containing biosolids from the activated sludge treatment basin. The sludge treatment system also includes an ozone-enriched gas injection system operatively coupled to the reactor and adapted to inject ozone-enriched gas into the liquid stream at or upstream of the sludge ozonation reactor. The sludge ozonation reactor is configured to allow effective gas-liquid contacting between the ozone-enriched gas and the liquid stream so as to oxidize the biosolids in the liquid stream and initiate bacterial cell lysis thereby reducing the biosolids. Upon reduction of the biosolids, the liquid stream is returned via a return line to the activated sludge basin or other discharge point.
摘要翻译： 公开了一种在废水处理工艺中通过臭氧处理和还原污泥的系统和方法。 污泥处理系统包括：与活性污泥处理池相连的污泥臭氧化反应器，适于从活性污泥处理池接收含有生物固体的污泥的液体流。 污泥处理系统还包括可操作地耦合到反应器的臭氧富集的气体注入系统，并且适于将臭氧富集的气体注入到污泥臭氧反应器中或上游的液体流中。 污泥臭氧化反应器被配置为允许在富含臭氧的气体和液体流之间有效的气液接触，以便使液体物流中的生物固体氧化并引发细菌细胞裂解从而减少生物固体。 在还原生物固体后，液流通过返回管线返回到活性污泥池或其他排放点。
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公开(公告)号：US20090075364A1
公开(公告)日：2009-03-19
申请号：US12271966
申请日：2008-11-17
CPC分类号： B01F3/04609 , B01F7/00358 , B01F7/0065 , B01F13/0049 , B01F2003/0456 , B01F2003/0468 , C02F3/1284 , C02F3/206 , Y02W10/15
摘要： A system and method for mixing high viscous liquids with gas is provided. The disclosed embodiments include a reactor or mixing vessel having a draft tube disposed therein, a gas injection subsystem adapted to inject gas into the reactor or mixing vessel proximate the entrance of the draft tube. The embodiments also include an agitator disposed within the draft tube which makes the draft tube the primary site for the gas-liquid mixing. In particular, the agitator is adapted to create gas bubbles having an average diameter between about 0.3 mm and 3.0 mm which are then ejected into the reactor or mixing vessel. The mass transfer efficiency associated with the present system and method is enhanced from the combined effect of gas dissolution into the high viscous liquid within the draft tube and greater bubble residence time within the high viscous liquid.
摘要翻译： 提供了一种用于将高粘度液体与气体混合的系统和方法。 所公开的实施例包括具有布置在其中的引流管的反应器或混合容器，适于将气体注入到靠近引流管入口的反应器或混合容器中的气体注入子系统。 实施例还包括设置在引流管内的搅拌器，其使引流管成为用于气液混合的主要部位。 特别地，搅拌器适于产生平均直径在约0.3mm至3.0mm之间的气泡，然后将其喷射到反应器或混合容器中。 与本系统和方法相关的传质效率从气体溶解到引流管内的高粘度液体和高粘滞液体中较大的气泡停留时间的组合效应增强。
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公开(公告)号：US07455776B2
公开(公告)日：2008-11-25
申请号：US11602519
申请日：2006-11-21
IPC分类号： C02F3/00
CPC分类号： B01F3/04609 , B01F7/00358 , B01F7/0065 , B01F13/0049 , B01F2003/0456 , B01F2003/0468 , C02F3/1284 , C02F3/206 , Y02W10/15
摘要： A system and method for mixing high viscous liquids with gas is provided. The disclosed embodiments include a reactor or mixing vessel having a draft tube disposed therein, a gas injection subsystem adapted to inject gas into the reactor or mixing vessel proximate the entrance of the draft tube. The embodiments also include an agitator disposed within the draft tube which makes the draft tube the primary site for the gas-liquid mixing. In particular, the agitator is adapted to create gas bubbles having an average diameter between about 0.3 mm and 3.0 mm which are then ejected into the reactor or mixing vessel. The mass transfer efficiency associated with the present system and method is enhanced from the combined effect of gas dissolution into the high viscous liquid within the draft tube and greater bubble residence time within the high viscous liquid.
摘要翻译： 提供了一种用于将高粘度液体与气体混合的系统和方法。 所公开的实施例包括具有布置在其中的引流管的反应器或混合容器，适于将气体注入到靠近引流管入口的反应器或混合容器中的气体注入子系统。 实施例还包括设置在引流管内的搅拌器，其使引流管成为用于气液混合的主要部位。 特别地，搅拌器适于产生平均直径在约0.3mm至3.0mm之间的气泡，然后将其喷射到反应器或混合容器中。 与本系统和方法相关的传质效率从气体溶解到引流管内的高粘度液体和高粘滞液体中较大的气泡停留时间的组合效应增强。
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公开(公告)号：US20080118946A1
公开(公告)日：2008-05-22
申请号：US11602519
申请日：2006-11-21
CPC分类号： B01F3/04609 , B01F7/00358 , B01F7/0065 , B01F13/0049 , B01F2003/0456 , B01F2003/0468 , C02F3/1284 , C02F3/206 , Y02W10/15
摘要： A system and method for mixing high viscous liquids with gas is provided. The disclosed embodiments include a reactor or mixing vessel having a draft tube disposed therein, a gas injection subsystem adapted to inject gas into the reactor or mixing vessel proximate the entrance of the draft tube. The embodiments also include an agitator disposed within the draft tube which makes the draft tube the primary site for the gas-liquid mixing. In particular, the agitator is adapted to create gas bubbles having an average diameter between about 0.3 mm and 3.0 mm which are then ejected into the reactor or mixing vessel. The mass transfer efficiency associated with the present system and method is enhanced from the combined effect of gas dissolution into the high viscous liquid within the draft tube and greater bubble residence time within the high viscous liquid.
摘要翻译： 提供了一种用于将高粘度液体与气体混合的系统和方法。 所公开的实施例包括具有布置在其中的引流管的反应器或混合容器，适于将气体注入到靠近引流管入口的反应器或混合容器中的气体注入子系统。 实施例还包括设置在引流管内的搅拌器，其使引流管成为用于气液混合的主要部位。 特别地，搅拌器适于产生平均直径在约0.3mm至3.0mm之间的气泡，然后将其喷射到反应器或混合容器中。 与本系统和方法相关的传质效率从气体溶解到引流管内的高粘度液体和高粘滞液体中较大的气泡停留时间的组合效应增强。
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公开(公告)号：US20080116132A1
公开(公告)日：2008-05-22
申请号：US11881845
申请日：2007-07-30
CPC分类号： B01F3/04609 , B01F7/00358 , B01F7/0065 , B01F13/0049 , B01F2003/0456 , B01F2003/0468 , C02F3/02 , C02F3/1284 , C02F3/165 , C02F3/206 , Y02W10/15
摘要： A system and method for oxygenating an aerobic sludge digester is provided. The disclosed embodiments include an aerobic sludge digester tank or vessel having a mechanically agitated contactor disposed therein, an oxygen injection subsystem adapted to inject oxygen into the digester tank proximate the mechanically agitated contactor. The embodiments of the mechanically agitated contactor include an agitator or impeller disposed within the draft tube which makes the draft tube the primary site for the gas-liquid mixing. In particular, the agitator or impeller is adapted to create gas bubbles having an average diameter between about 0.3 mm and 3.0 mm which are then dispersed into the aerobic digester. The mass transfer efficiency associated with the present system and method is enhanced from the combined effect of oxygen dissolution into the sludge and greater bubble residence time.
摘要翻译： 本发明提供一种氧气污泥消化器的氧化系统和方法。 所公开的实施例包括一个好氧污泥消化器罐或容器，其中设置有机械搅拌的接触器，氧气注入子系统适于将氧气注入靠近机械搅拌接触器的蒸煮罐中。 机械搅拌的接触器的实施例包括设置在引流管内的搅拌器或叶轮，其使引流管成为用于气液混合的主要部位。 特别地，搅拌器或叶轮适于产生平均直径在约0.3mm至3.0mm之间的气泡，然后将其分散到需氧消化器中。 与现有系统和方法相关的传质效率从氧气溶解到污泥中的联合效应和较大的气泡停留时间得到提高。
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9.发明授权公开(公告)号：US07513999B2
公开(公告)日：2009-04-07
申请号：US11880694
申请日：2007-07-24
IPC分类号： C02F3/00
CPC分类号： C02F3/12 , C02F1/78 , C02F3/1221 , C02F2209/06 , C02F2303/06 , C02F2303/12 , Y02W10/15
摘要： A system and method for the ozone treatment of wastewater is disclosed. The disclosed wastewater treatment system includes a high selectivity reactor coupled to an activated sludge treatment basin. The high selectivity reactor is adapted to receive a stream containing sludge diverted directly or indirectly from the activated sludge treatment basin. The disclosed wastewater treatment system and method is adapted to inject a chemical agent, such as ozone-enriched gas, into the diverted stream for treatment within the high selectivity reactor for purposes of sludge reduction, foam control, or bulking control. The treated stream is then returned to the activated sludge treatment basin.
摘要翻译： 公开了臭氧处理废水的系统和方法。 公开的废水处理系统包括与活性污泥处理池相连的高选择性反应器。 高选择性反应器适于接收含有从活性污泥处理池直接或间接转移的污泥的物流。 所公开的废水处理系统和方法适于在用于污泥减少，泡沫控制或膨胀控制的目的的高选择性反应器内将用于诸如富含臭氧的气体的化学试剂注入到转向流中用于处理。 然后将处理过的物流返回到活性污泥处理池。
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10.发明申请公开(公告)号：US20080105614A1
公开(公告)日：2008-05-08
申请号：US11880694
申请日：2007-07-24
IPC分类号： C02F3/12
CPC分类号： C02F3/12 , C02F1/78 , C02F3/1221 , C02F2209/06 , C02F2303/06 , C02F2303/12 , Y02W10/15
摘要： A system and method for the ozone treatment of wastewater is disclosed. The disclosed wastewater treatment system includes a high selectivity reactor coupled to an activated sludge treatment basin. The high selectivity reactor is adapted to receive a stream containing sludge diverted directly or indirectly from the activated sludge treatment basin. The disclosed wastewater treatment system and method is adapted to inject a chemical agent, such as ozone-enriched gas, into the diverted stream for treatment within the high selectivity reactor for purposes of sludge reduction, foam control, or bulking control. The treated stream is then returned to the activated sludge treatment basin.
摘要翻译： 公开了臭氧处理废水的系统和方法。 公开的废水处理系统包括与活性污泥处理池相连的高选择性反应器。 高选择性反应器适于接收含有从活性污泥处理池直接或间接转移的污泥的物流。 所公开的废水处理系统和方法适于在用于污泥减少，泡沫控制或膨胀控制的目的的高选择性反应器内将用于诸如富含臭氧的气体的化学试剂注入到转向流中用于处理。 然后将处理过的物流返回到活性污泥处理池。
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