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公开(公告)号：US08057676B2
公开(公告)日：2011-11-15
申请号：US12303510
申请日：2007-05-17
IPC分类号： C02F3/00
CPC分类号： C02F3/06 , C02F1/283 , C02F3/34 , C02F3/348 , C02F2101/14 , C02F2103/346 , C02F2305/06 , Y02W10/15
摘要： Drainage water containing an organofluorine compound is introduced into a raw tank (1) and then filtered through a filtration device (4). Next, a microorganism, a micro-nanobubbling auxiliary agent and a nutrient are added thereto in a first transit tank (5) while micro-nanobubbles are generated thereinto by a micro-nanobubbling machine (7), thereby giving treated water. This treated water is then fed into an active carbon column (14) and then the above-described organofluorine compound contained in the treated water is decomposed by the microorganism as described above.
摘要翻译： 将含有有机氟化合物的排水引入原料罐（1）中，然后通过过滤装置（4）过滤。 接下来，在第一转运槽（5）中向其中加入微生物，微纳米球形辅助剂和营养物，同时通过微纳米沉淀机（7）在其中产生微纳泡，由此得到处理水。 然后将该处理过的水加入到活性碳柱（14）中，然后如上所述，由处理水中包含的上述有机氟化合物被微生物分解。
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公开(公告)号：US07803272B2
公开(公告)日：2010-09-28
申请号：US11992156
申请日：2006-02-28
IPC分类号： B01D33/70
CPC分类号： C02F1/28 , C02F3/006 , C02F3/108 , C02F3/20 , C02F3/30 , C02F2209/04 , C02F2209/22 , C02F2301/046 , C02F2303/26 , Y02W10/15
摘要： A first treatment tank (1) to a fourth treatment tank are installed prior to ultrapure water production apparatus (5), dilute wastewater recovering apparatus (34), general service water recovering apparatus and wastewater treatment apparatus. The treatment tanks (1, 2, . . . ) each have a micro-nano bubble generation tank (6, 23, . . . ) and an anaerobic measuring tank (7, 24, . . . ). Accordingly, microbes within the respective anaerobic measuring tanks (7, 24, . . . ) are activated by micro-nano bubbles generated in each micro-nano bubble generation tank (6, 23, . . . ) to thereby enhance the treatment efficiency of low-concentration organic matter. Further, when the value measured by dissolved oxygen meter (13, 30, . . . ) or oxidation-reduction potentiometer (14, 31, . . . ) of each anaerobic measuring tank (7, 24, . . . ) exceeds an individually determined given range, the rotational speed of a circulating pump (9, 26, . . . ) is controlled to thereby decrease the generation of micro-nano bubbles. Thus, the micro-nano bubble content in water undergoing treatment is held appropriate.
摘要翻译： 在超纯水生产设备（5），稀释废水回收设备（34），一般服务水回收设备和废水处理设备之前，安装第一处理槽（1）至第四处理槽。 处理罐（1,2）各自具有微纳米泡沫生成罐（6,23 ...）和厌氧测量罐（7,24 ...）。 因此，各个厌氧测量罐（7,24 ...）内的微生物通过在每个微纳米泡沫生成罐（6,23 ...）中产生的微纳米气泡而被活化，从而提高了处理效率 低浓度有机物质。 此外，当每个厌氧测量罐（7,24，...）的溶解氧计（13,30，...）或氧化还原电位计（14,31，...）测量的值超过单独 确定给定范围，控制循环泵（9,26 ...）的旋转速度，从而减少微纳米气泡的产生。 因此，正在进行处理的水中的微纳米气泡含量是适当的。
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3.发明授权Manufacturing device and application device for liquid containing micro-nano bubbles 有权含微量纳米气泡的液体的制造装置和应用装置公开(公告)号：US07628912B2
公开(公告)日：2009-12-08
申请号：US11896542
申请日：2007-09-04
IPC分类号： C02F3/00
CPC分类号： B01F3/0451 , A01K63/042 , B01F3/04531 , B01F3/04985 , B01F5/106 , B01F13/1025 , B01F13/1038 , B01F15/00155 , B01F15/00207 , B01F15/00253 , B01F15/00344 , B08B3/10 , C02F1/74 , C02F3/20 , C02F2209/005 , C02F2209/11 , C02F2209/42 , Y02W10/15
摘要： The application device for liquid containing micro-nano bubbles generates micro-nano bubbles in a wide size distribution with use of a submerged pump-type micro-nano bubble generator and a spiral flow-type micro-nano bubble generator. A micro-nano bubble generating aid metering pump is controlled by a bubble level meter and a level controller, so that the supply amount of a micro-nano bubble generating aid is controlled in response to the level of bubbles from a fluid level. The supply amount of a micro-nano bubble generating aid is also controlled by a turbidimeter and a controller in response to the turbidity of the liquid in a micro-nano bubble generation tank, while the amount of air supplied to the submerged pump-type micro-nano bubble generator is controlled in response to the turbidity of the liquid. Therefore, the device can produce a large amount of various micro-nano bubbles in a wide size distribution more economically.
摘要翻译： 用于含有微纳米气泡的液体的应用装置使用浸没式泵型微纳米气泡发生器和螺旋流型微纳米气泡发生器产生宽尺寸分布的微纳米气泡。 微气泡生成助剂计量泵由气泡量表和液位控制器控制，从而响应于来自液位的气泡水平来控制微纳米气泡发生助剂的供应量。 微纳米发泡助剂的供给量也由浊度计和控制器响应于微纳米气泡生成槽中的液体的浊度而被控制，同时供给到浸没式泵型微孔的空气量 纳米气泡发生器是响应于液体的浊度而被控制的。 因此，该装置可以更经济地产生大尺寸分布的大量各种微纳米气泡。
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公开(公告)号：US20090145827A1
公开(公告)日：2009-06-11
申请号：US11992156
申请日：2006-02-28
CPC分类号： C02F1/28 , C02F3/006 , C02F3/108 , C02F3/20 , C02F3/30 , C02F2209/04 , C02F2209/22 , C02F2301/046 , C02F2303/26 , Y02W10/15
摘要： A first treatment tank (1) to a fourth treatment tank are installed prior to ultrapure water production apparatus (5), dilute wastewater recovering apparatus (34), general service water recovering apparatus and wastewater treatment apparatus. The treatment tanks (1, 2, . . . ) each have a micro-nano bubble generation tank (6, 23, . . . ) and an anaerobic measuring tank (7, 24, . . . ). Accordingly, microbes within the respective anaerobic measuring tanks (7, 24, . . . ) are activated by micro-nano bubbles generated in each micro-nano bubble generation tank (6, 23, . . . ) to thereby enhance the treatment efficiency of low-concentration organic matter. Further, when the value measured by dissolved oxygen meter (13, 30, . . . ) or oxidation-reduction potentiometer (14, 31, . . . ) of each anaerobic measuring tank (7, 24, . . . ) exceeds an individually determined given range, the rotational speed of a circulating pump (9, 26, . . . ) is controlled to thereby decrease the generation of micro-nano bubbles. Thus, the micro-nano bubble content in water undergoing treatment is held appropriate.
摘要翻译： 在超纯水生产设备（5），稀释废水回收设备（34），一般服务水回收设备和废水处理设备之前，安装第一处理槽（1）至第四处理槽。 处理罐（1,2）各自具有微纳米泡沫生成罐（6,23 ...）和厌氧测量罐（7,24 ...）。 因此，各个厌氧测量罐（7,24 ...）内的微生物通过在每个微纳米泡沫生成罐（6,23 ...）中产生的微纳米气泡而被活化，从而提高了处理效率 低浓度有机物质。 此外，当每个厌氧测量罐（7,24，...）的溶解氧计（13,30，...）或氧化还原电位计（14,31，...）测量的值超过单独 确定给定范围，控制循环泵（9,26 ...）的旋转速度，从而减少微纳米气泡的产生。 因此，正在进行处理的水中的微纳米气泡含量是适当的。
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5.发明授权Apparatus for treatment of waste water and/or exhaust gases containing fluorine and surface active agents 失效用于处理含氟和表面活性剂的废水和/或废气的设备
公开(公告)号：US5702594A
公开(公告)日：1997-12-30
申请号：US465755
申请日：1995-06-06
IPC分类号： C02F3/04 , C02F1/20 , C02F1/28 , C02F1/52 , C02F1/56 , C02F1/58 , C02F3/06 , C02F3/10 , C02F9/00 , C02F11/12
CPC分类号： C02F1/281 , C02F1/583 , C02F3/043 , C02F2101/14 , Y02W10/15 , Y10S210/915
摘要： A first reaction/adjustment tank has a lower portion containing a calcium carbonate mineral, an upper portion containing a calcium carbonate mineral and a plastic filler, and an air lift pump for circulating waste water from the lower portion to the upper portion. Exhaust gas is introduced into a space. A second reaction/adjustment tank has a lower portion containing a calcium carbonate mineral and charcoal, and an upper portion containing charcoal and a plastic filler. Waste water circulates sequentially through the lower and upper portions of the first reaction/adjustment tank, and the lower and upper portions of the second reaction/adjustment tank. Exhaust gas circulates sequentially through the upper portion of the first reaction/adjustment tank and the upper portion of the second reaction/adjustment tank.
摘要翻译： 第一反应/调节罐具有含有碳酸钙矿物的下部，含有碳酸钙矿物的上部和塑料填料，以及用于使废水从下部循环到上部的空气提升泵。 废气被引入空间。 第二反应/调节罐具有含有碳酸钙矿物和活性炭的下部，以及含有木炭和塑料填料的上部。 废水依次通过第一反应/调节罐的下部和上部以及第二反应/调节罐的下部和上部。 排气顺序地循环通过第一反应/调节罐的上部和第二反应/调节罐的上部。
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6.发明授权
公开(公告)号：US5580458A
公开(公告)日：1996-12-03
申请号：US452400
申请日：1995-05-26
申请人： Kazuyuki Yamasaki , Yoshihiro Hamaguchi , Shunji Hosoda , Kazuyuki Sakata , Takashi Imai , Shigetoshi Okatani , Satoshi Nishio , Tuyoshi Takahashi , Kenji Matuura , Noriyuki Tanaka , Teruaki Nagayasu , Hiroshi Makino
发明人： Kazuyuki Yamasaki , Yoshihiro Hamaguchi , Shunji Hosoda , Kazuyuki Sakata , Takashi Imai , Shigetoshi Okatani , Satoshi Nishio , Tuyoshi Takahashi , Kenji Matuura , Noriyuki Tanaka , Teruaki Nagayasu , Hiroshi Makino
CPC分类号： C02F3/34 , C02F1/5236 , C02F1/583 , C02F3/10 , Y02W10/15 , Y10S210/915
摘要： An apparatus for waste water treatment, wherein fluorine contained in waste water is treated into a fluoride through a chemical reaction and sludge containing the fluoride is thickened and dehydrated into a sludge cake, has first and second tanks each packed with calcium carbonate mineral. In the first tank, waster water containing fluorine is agitated by air discharged from an air diffuser and caused to react with the calcium carbonate mineral. Through this reaction of the waste water with the calcium carbonate mineral and action of microorganisms on the surface of the calcium carbonate mineral, a pH value and a fluorine concentration of the waste water is adjusted till the pH value and the fluorine concentration fall within their respective predetermined ranges. In the second tank, an aluminum agent is added to the waste water coming from the first tank while the waste water being agitated so that the pH value and the fluorine concentration of the waste water are further adjusted through a chemical reaction of the fluorine with the calcium carbonate mineral and aluminum agent and action of microorganisms propagating on the surface of the mineral so as to fall within their respective target ranges.
摘要翻译： 一种用于废水处理的设备，其中通过化学反应将废水中所含的氟处理成氟化物，并且将含有氟化物的污泥增稠并脱水至污泥饼中，其中，第一和第二罐各自填充有碳酸钙矿物。 在第一罐中，含有氟的废水被从空气扩散器排出的空气搅拌并与碳酸钙矿物反应。 通过废水与碳酸钙矿物的反应和微生物对碳酸钙矿物表面的作用，调节pH值和废水的氟浓度，直到pH值和氟浓度落入其各自的 预定范围。 在第二罐中，在来自第一罐的废水中加入铝剂，同时搅拌废水，通过氟与氟化物的化学反应进一步调节废水的pH值和氟浓度 碳酸钙矿物和铝剂以及在矿物表面上传播的微生物的作用落入其各自的目标范围内。
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公开(公告)号：US08043848B2
公开(公告)日：2011-10-25
申请号：US11783671
申请日：2007-04-11
CPC分类号： C12M27/02 , B01F2215/0073 , C12M29/02 , C12M29/06 , C12M37/02
摘要： In a bioreactor, a culture solution derived from a cultivation tank is separated into bacteria cells and filtrate by a bacteria cell filter. The filtrate is introduced from the bacteria cell filter into a micro-nano bubble generation tank where micro-nano-bubbles are mixed with the filtrate. The filtrate containing micro-nano-bubbles is returned to the cultivation tank to activate the microorganisms therein, so that a biological reaction time is reduced by the activated microorganisms.
摘要翻译： 在生物反应器中，将来自培养槽的培养液分离成细菌细胞并用细菌细胞过滤器滤液。 将滤液从细菌细胞过滤器引入到微纳米气泡生成罐中，其中将微纳米气泡与滤液混合。 将含有微纳米气泡的滤液返回到培养槽中以活化其中的微生物，从而通过活化的微生物降低生物反应时间。
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公开(公告)号：US20090152193A1
公开(公告)日：2009-06-18
申请号：US12303510
申请日：2007-05-17
IPC分类号： C02F3/00 , C02F101/36
CPC分类号： C02F3/06 , C02F1/283 , C02F3/34 , C02F3/348 , C02F2101/14 , C02F2103/346 , C02F2305/06 , Y02W10/15
摘要： Drainage water containing an organofluorine compound is introduced into a raw tank (1) and then filtered through a filtration device (4). Next, a microorganism, a micro-nanobubbling auxiliary agent and a nutrient are added thereto in a first transit tank (5) while micro-nanobubbles are generated thereinto by a micro-nanobubbling machine (7), thereby giving treated water. This treated water is then fed into an active carbon column (14) and then the above-described organofluorine compound contained in the treated water is decomposed by the microorganism as described above.
摘要翻译： 将含有有机氟化合物的排水引入原料罐（1）中，然后通过过滤装置（4）过滤。 接下来，在第一转运槽（5）中向其中加入微生物，微纳米球形辅助剂和营养物，同时通过微纳米沉淀机（7）在其中产生微纳泡，由此得到处理水。 然后将该处理过的水加入到活性碳柱（14）中，然后如上所述，由处理水中包含的上述有机氟化合物被微生物分解。
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9.发明申请Manufacturing method for micro-nano bubble bathtub water and micro-nano bubble bathtub 有权微纳米泡泡浴缸水和微纳米泡泡浴缸的制造方法公开(公告)号：US20080189847A1
公开(公告)日：2008-08-14
申请号：US11896544
申请日：2007-09-04
IPC分类号： A61H33/02
CPC分类号： A61H33/02 , A61H33/027 , A61H33/6026 , A61H33/6036 , A61H33/6073 , A61H2033/0037
摘要： In the upper part and the lower part of a micro-nano bubble generation section 34 in a micro-nano bubble bathtub 1, two kinds of micro-nano bubbles different in a size distribution are generated by first and second micro-nano bubble generators (submerged pump-type micro-nano bubble generator 2 and spiral flow-type micro-nano bubble generator 10) of two kinds, so that bathtub water containing micro-nano bubbles in a wide size distribution can be produced in a large amount. Some of the water containing micro-nano bubbles generated in the lower part is thrown into the first micro-nano bubble generator (spiral flow-type micro-nano bubble generator 10) in the upper part, so that the spiral flow-type micro-nano bubble generator 10 can generate micro-nano bubbles in a smaller size. Therefore, in this bathtub, micro-nano bubbles abundant in size and large in amount can be produced economically.
摘要翻译： 在微纳米泡沫浴缸1中的微纳米泡沫产生部分34的上部和下部，通过第一和第二微纳米气泡发生器产生尺寸分布不同的两种微纳米气泡（ 淹水泵型微纳米泡沫发生器2和螺旋流式微纳米气泡发生器10）两种，使得可以大量生产含有大尺寸分布的微纳米气泡的浴缸水。 在下部产生的含有微纳米泡沫的一些水被投入到上部的第一微纳米气泡发生器（螺旋流型微纳米气泡发生器10）中，使得螺旋流型微 - 纳米气泡发生器10可以产生更小尺寸的微纳米气泡。 因此，在该浴缸中，可以经济地制造尺寸大，量大的微纳米气泡。
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公开(公告)号：US20070275452A1
公开(公告)日：2007-11-29
申请号：US11783671
申请日：2007-04-11
CPC分类号： C12M27/02 , B01F2215/0073 , C12M29/02 , C12M29/06 , C12M37/02
摘要： In a bioreactor, a culture solution derived from a cultivation tank is separated into bacteria cells and filtrate by a bacteria cell filter. The filtrate is introduced from the bacteria cell filter into a micro-nano bubble generation tank where micro-nano-bubbles are mixed with the filtrate. The filtrate containing micro-nano-bubbles is returned to the cultivation tank to activate the microorganisms therein, so that a biological reaction time is reduced by the activated microorganisms.
摘要翻译： 在生物反应器中，将来自培养槽的培养液分离成细菌细胞并用细菌细胞过滤器滤液。 将滤液从细菌细胞过滤器引入到微纳米气泡生成罐中，其中将微纳米气泡与滤液混合。 将含有微纳米气泡的滤液返回到培养槽中以活化其中的微生物，从而通过活化的微生物降低生物反应时间。
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