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    • 3. 发明申请
    • Module cleaning method
    • 模块清洗方法
    • US20070075021A1
    • 2007-04-05
    • US10595841
    • 2004-11-12
    • Warren Johnson
    • Warren Johnson
    • B01D65/02
    • B01D61/18B01D63/02B01D63/046B01D65/02B01D65/08B01D2313/02B01D2313/20B01D2313/26B01D2315/06B01D2317/04B01D2321/02B01D2321/04B01D2321/12B01D2321/14B01D2321/18B01D2321/185
    • An aeration/backwash device (16) for use with a porous membrane filtration module (5) including one or more membranes (6) extending longitudinally between vertically spaced upper (7) and lower headers (8) into which the ends of the membranes are potted. The membranes (6) having a permeable wall which, in use, is subjected to a filtration operation wherein feed containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall. The aeration/backwash device (16) adapted to at least partially surround a portion of said membrane module (5) and including a communication chamber (17) having spaced through-openings (18, 19) in fluid communication with the chamber (17) and the membrane module (5). In use, gas is supplied to the chamber (17) and communicated to the membrane module (5) through the through-openings (18, 19) to aerate the membranes within the membrane module and liquid backwash is withdrawn from and/or fed into the membrane module (5) through the throughopenings into the chamber (17).
    • 一种用于多孔膜过滤模块(5)的曝气/回洗装置(16),包括一个或多个膜(6),纵向间隔开的上部(7)和下部集管(8)之间纵向延伸,膜的端部 盆栽。 具有渗透壁的膜(6)在使用中进行过滤操作,其中将含有污染物质的进料施加到膜壁的一侧并且滤液从膜壁的另一侧排出。 曝气/反冲洗装置(16),其适于至少部分地围绕所述膜组件(5)的一部分并且包括具有与所述腔室(17)流体连通的间隔开通孔(18,19)的连通腔室(17) 和膜组件(5)。 在使用中,将气体供应到室(17)并且通过通孔(18,19)连通到膜组件(5),以使膜组件内的膜充气,并且液体反冲洗从和/或进入 所述膜组件(5)通过所述节流孔进入所述腔室(17)。
    • 6. 发明授权
    • Water purifier system and valve
    • 净水器系统和阀门
    • US4176063A
    • 1979-11-27
    • US844374
    • 1977-10-21
    • Truman V. Tyler
    • Truman V. Tyler
    • C02F1/44A61L2/00B01D61/02B01D61/08B01D61/10B01D61/12B01D63/00B01D65/02F16K7/14C02B1/82
    • B01D61/08B01D65/02B01D2313/18B01D2313/50B01D2321/12B01D2321/14
    • An economical and commercially practical reverse-osmosis water purifier system which has no back pressure acting against the semipermeable membrane, so that the filtering rate is maximized. Furthermore, the supply of tap water to the system is shut off automatically as soon as the pure water storage tank is full, use of water thus being greatly reduced. These, and other major advantages, are achieved despite the fact that there is only a single tube extending to the faucet, automatic ice-maker, refrigerated drinking fountain or other point of use.The system uses rugged, long-lasting and economical diaphragm valves, which eliminates the need for sliding seals. Thus, it becomes highly practical to injection-mold the valves of plastic.The long-standing major problem of plugging or fouling of the constricted outlet for waste water is eliminated at low cost and with very little use of water. What water is used provides not only cleaning of the constriction region but also a partial flushing of the filter membrane. These results are achieved by means of a self-cleaning constrictor valve having a predetermined flow area which may be made as small as the manufacturer desires.In one embodiment, a valve is provided to automatically stop the outflow of squeeze water while the faucet is in open condition. This saves additional water and also makes it possible to build up a relatively high pure-water pressure even when the inlet pressure is less than average.
    • 一种经济且商业上实用的反渗透净水器系统,其无反压力作用于半透膜,从而使过滤速率最大化。 此外,一旦纯净水储存罐充满,系统自来水的供应便会自动关闭,从而大大减少了使用水量。 尽管事实上只有一根管延伸到水龙头,自动制冰机,冷藏饮水机或其他使用点上,但是这些和其他主要的优点是实现的。 该系统采用坚固耐用,经久耐用的隔膜阀,无需滑动密封。 因此,注塑塑料阀门变得非常实用。 废水的收缩出口堵塞或堵塞的长期存在的主要问题是以低成本且少量使用水被消除。 使用什么水不仅提供收缩区域的清洁,而且还可以部分地冲洗过滤膜。 这些结果通过具有预定流动面积的自清洁压缩阀来实现,该预定的流动区域可以制造得像制造商所希望的那样小。 在一个实施例中,阀被设置成在水龙头处于打开状态时自动停止挤压水的流出。 这节省了额外的水,并且即使当入口压力小于平均值时,也可以建立相对较高的纯水压力。
    • 7. 发明授权
    • Enzymatic treatment of alginate to reduce membrane fouling for water or wastewater purification
    • 藻酸盐的酶法处理以减少水污染或污水净化的膜污染
    • US09352284B2
    • 2016-05-31
    • US13552746
    • 2012-07-19
    • Dong Chen
    • Dong Chen
    • B01D61/00B01D65/02C02F1/44B01D65/08B01D61/14
    • B01D65/08B01D61/145B01D61/147B01D65/02B01D2321/04B01D2321/14B01D2321/166
    • This disclosure examines using alginate lyase to catalytically degrade alginate in order to decrease affinity and fouling potential to membranes of 0.2 and 0.02 μm pore size, respectively within a process line of a filtration system. Enzymatically treated alginate caused less fouling on both ultrafiltration and microfiltration membranes than original alginate. Enzymatically treated alginate is predicted to cause less fouling on both membranes within the pH range of approximately 3.0 to approximately 10.0. Without the presence of calcium cation, alginate lyase reduced the foulant resistance by more than 82% for both membranes. In the presence of 1 mM calcium cation, alginate lyase reduced the foulant resistance by more than 55%. In addition, the foulant structure composed of enzymatically treated alginate was more readily removed by backwashing, suggesting reversible fouling. The advantages of using enzymatic technique to control membrane fouling include high efficiency and no damage to the membrane materials.
    • 该公开内容检查了使用藻酸盐裂解酶来催化降解海藻酸盐,以便分别在过滤系统的生产线中降低亲和力并将潜在的污垢污染至0.2和0.02μm孔径的膜。 酶处理的藻酸盐在超滤和微滤膜上比原始藻酸盐引起的污垢较少。 预计酶处理的藻酸盐在约3.0至约10.0的pH范围内在两个膜上引起较少的结垢。 没有钙阳离子的存在,藻酸盐裂解酶使两种膜的抗污性降低了82%以上。 在1mM钙阳离子存在下,藻酸盐裂解酶可使阻垢剂抗性降低55%以上。 此外,由酶处理的藻酸盐组成的污垢结构通过反冲洗更容易除去,这表明可逆的结垢。 使用酶法技术控制膜污染的优点包括效率高,不会损坏膜材料。
    • 9. 发明申请
    • ENZYMATIC TREATMENT OF ALGINATE TO REDUCE MEMBRANE FOULING FOR WATER OR WASTEWATER PURIFICATION
    • 用于水或废水净化的氧化铝减少膜的热处理
    • US20130037484A1
    • 2013-02-14
    • US13552746
    • 2012-07-19
    • Dong Chen
    • Dong Chen
    • B01D65/02
    • B01D65/08B01D61/145B01D61/147B01D65/02B01D2321/04B01D2321/14B01D2321/166
    • This disclosure examines using alginate lyase to catalytically degrade alginate in order to decrease affinity and fouling potential to membranes of 0.2 and 0.02 μm pore size, respectively within a process line of a filtration system. Enzymatically treated alginate caused less fouling on both ultrafiltration and microfiltration membranes than original alginate. Enzymatically treated alginate is predicted to cause less fouling on both membranes within the pH range of approximately 3.0 to approximately 10.0. Without the presence of calcium cation, alginate lyase reduced the foulant resistance by more than 82% for both membranes. In the presence of 1 mM calcium cation, alginate lyase reduced the foulant resistance by more than 55%. In addition, the foulant structure composed of enzymatically treated alginate was more readily removed by backwashing, suggesting reversible fouling. The advantages of using enzymatic technique to control membrane fouling include high efficiency and no damage to the membrane materials.
    • 该公开内容检查了使用藻酸盐裂解酶来催化降解海藻酸盐,以便分别在过滤系统的生产线中降低亲和力并将潜在的污垢污染至0.2和0.02μm孔径的膜。 酶处理的藻酸盐在超滤和微滤膜上比原始藻酸盐引起的污垢较少。 预计酶处理的藻酸盐在约3.0至约10.0的pH范围内在两个膜上引起较少的结垢。 没有钙阳离子的存在,藻酸盐裂解酶使两种膜的抗污性降低了82%以上。 在1mM钙阳离子存在下,藻酸盐裂解酶可使阻垢剂抗性降低55%以上。 此外,由酶处理的藻酸盐组成的污垢结构通过反冲洗更容易除去,这表明可逆的结垢。 使用酶法技术控制膜污染的优点包括效率高,不会损坏膜材料。
    • 10. 发明授权
    • Module cleaning method
    • 模块清洗方法
    • US08808540B2
    • 2014-08-19
    • US10595841
    • 2004-11-12
    • Warren Thomas Johnson
    • Warren Thomas Johnson
    • B01D65/02
    • B01D61/18B01D63/02B01D63/046B01D65/02B01D65/08B01D2313/02B01D2313/20B01D2313/26B01D2315/06B01D2317/04B01D2321/02B01D2321/04B01D2321/12B01D2321/14B01D2321/18B01D2321/185
    • An aeration/backwash device (16) for use with a porous membrane filtration module (5) including one or more membranes (6) extending longitudinally between vertically spaced upper (7) and lower headers (8) into which the ends of the membranes are potted. The membranes (6) having a permeable wall which, in use, is subjected to a filtration operation wherein feed containing contaminant matter is applied to one side of the membrane wall and filtrate is withdrawn from the other side of the membrane wall. The aeration/backwash device (16) adapted to at least partially surround a portion of said membrane module (5) and including a communication chamber (17) having spaced through-openings (18, 19) in fluid communication with the chamber (17) and the membrane module (5). In use, gas is supplied to the chamber (17) and communicated to the membrane module (5) through the through-openings (18, 19) to aerate the membranes within the membrane module and liquid backwash is withdrawn from and/or fed into the membrane module (5) through the throughopenings into the chamber (17).
    • 一种用于多孔膜过滤模块(5)的曝气/回洗装置(16),包括一个或多个膜(6),纵向间隔开的上部(7)和下部集管(8)之间纵向延伸,膜的端部 盆栽。 具有渗透壁的膜(6)在使用中进行过滤操作,其中将含有污染物质的进料施加到膜壁的一侧并且滤液从膜壁的另一侧排出。 曝气/反冲洗装置(16),其适于至少部分地围绕所述膜组件(5)的一部分并且包括具有与所述腔室(17)流体连通的间隔开通孔(18,19)的连通腔室(17) 和膜组件(5)。 在使用中,将气体供应到室(17)并且通过通孔(18,19)连通到膜组件(5),以使膜组件内的膜充气,并且液体反冲洗从和/或进入 所述膜组件(5)通过所述节流孔进入所述腔室(17)。