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公开(公告)号：US11207613B2
公开(公告)日：2021-12-28
申请号：US16914548
申请日：2020-06-29
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
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公开(公告)号：US09643862B2
公开(公告)日：2017-05-09
申请号：US14219951
申请日：2014-03-19
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
CPC classification number: C02F1/42 , B01D15/02 , B01J47/10 , B01J47/14 , B01J49/10 , B01J49/12 , B01J49/14 , B01J49/85 , C02F2001/422 , C02F2001/425 , C02F2209/005 , C02F2209/006 , C02F2209/03 , C02F2209/05 , C02F2209/06 , C02F2209/40 , C02F2303/16
Abstract: Methods and apparatus for removing contaminants from liquid using a continuously circulating stream of purifying media are disclosed. In one embodiment the method includes mixing a regenerated purifying media with a contaminated liquid containing diverse contaminants; co-currently transporting the purifying media and the contaminated liquid in a mixed state; removing, using the purifying media, while co-currently transporting the purifying media and the contaminated liquid, contaminants from the contaminated liquid so as to produce a mixture of a decontaminated liquid and a contaminated purifying media; and separating contaminated purifying media from the decontaminated liquid. In addition, the contaminated purifying media is contacted in counter current fashion with a regenerant solution so as to produce a regenerated purifying media and the regenerated purifying media is returned to the mixing step, whereby the continuously circulating purifying media selectively removes contaminants from the liquid.
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公开(公告)号：US20200324222A1
公开(公告)日：2020-10-15
申请号：US16914548
申请日：2020-06-29
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
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公开(公告)号：US09714178B2
公开(公告)日：2017-07-25
申请号：US14604067
申请日：2015-01-23
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
IPC: C02F1/28 , B01D15/02 , B01J20/08 , C02F101/10
CPC classification number: C02F1/281 , B01D15/02 , B01J20/08 , C02F2101/10 , C02F2209/006 , C02F2209/008 , C02F2209/03 , C02F2209/06 , C02F2303/16
Abstract: Treatment of silica-laden wastewater is herein described. Unlike traditional fixed bed designs that cannot use an activated alumina sorbent due to the high volumes of sorbent needed in a fixed bed design, the herein disclosed continuous cycle enables smaller volumes of sorbent to be used and thereby enabling activated alumina to be used. Adsorption, regeneration, and rinse regions are provided. Activated alumina is provided to the adsorption region along with silica-containing wastewater. A pH below the zero point charge for alumina is set, and this causes the silica to load onto the alumina. Gravity brings the loaded alumina to the regeneration region, having a pH equal to or greater than the zero point charge of alumina such that the silica is released from the alumina. The silica and alumina are further separated in the rinse region, and the regenerated alumina can then be returned to the adsorption region.
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公开(公告)号：US10737197B2
公开(公告)日：2020-08-11
申请号：US15914426
申请日：2018-03-07
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
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Patent Agency Ranking
6.发明申请公开(公告)号：US20160230483A1
公开(公告)日：2016-08-11
申请号：US15010890
申请日：2016-01-29
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
CPC classification number: B01D11/0223 , B01D11/0242 , B01D11/0253 , B01D21/0045 , B01D21/245
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
Abstract translation: 本公开描述用于逆流固体浸出的系统，方法和装置。 多级逆流浸出室可以包括顶端和底端，贫液输入，用于逆流混合的两个或更多个区域和贫固体输出。 输入可配置为接收贫瘠酒。 用于逆流混合和分离的两个或更多个区域可以被配置为混合和分离液相和固相。 贫固体输出可以被配置为从多级逆流浸出室的底端收集和排出贫瘠的固体。 还可以包括流化床室和澄清器室，其中流化床接收怀疑固体的可流化淤浆，澄清器室有助于将液体与从流化床室顶部通过多层流化床顶部的固体分离， 阶段逆流浸出室。
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7.发明申请公开(公告)号：US20150203367A1
公开(公告)日：2015-07-23
申请号：US14604067
申请日：2015-01-23
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
CPC classification number: C02F1/281 , B01D15/02 , B01J20/08 , C02F2101/10 , C02F2209/006 , C02F2209/008 , C02F2209/03 , C02F2209/06 , C02F2303/16
Abstract: Treatment of silica-laden wastewater is herein described. Unlike traditional fixed bed designs that cannot use an activated alumina sorbent due to the high volumes of sorbent needed in a fixed bed design, the herein disclosed continuous cycle enables smaller volumes of sorbent to be used and thereby enabling activated alumina to be used. Adsorption, regeneration, and rinse regions are provided. Activated alumina is provided to the adsorption region along with silica-containing wastewater. A pH below the zero point charge for alumina is set, and this causes the silica to load onto the alumina. Gravity brings the loaded alumina to the regeneration region, having a pH equal to or greater than the zero point charge of alumina such that the silica is released from the alumina. The silica and alumina are further separated in the rinse region, and the regenerated alumina can then be returned to the adsorption region.
Abstract translation: 本文描述了处理含二氧化硅的废水。 与传统的固定床设计不同，传统的固定床设计由于固定床设计中所需的大量吸附剂而不能使用活性氧化铝吸附剂，本文公开的连续循环使得能够使用更小体积的吸附剂，从而使活性氧化铝得以使用。 提供吸附，再生和冲洗区域。 活性氧化铝与含二氧化硅的废水一起提供给吸附区域。 低于氧化铝的零点电荷的pH被设定，这导致二氧化硅负载到氧化铝上。 重量将负载的氧化铝带到再生区域，其pH值等于或大于氧化铝的零点电荷，使二氧化硅从氧化铝中释放出来。 在漂洗区域进一步分离二氧化硅和氧化铝，然后将再生的氧化铝返回到吸附区域。
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公开(公告)号：US20190076754A1
公开(公告)日：2019-03-14
申请号：US15914426
申请日：2018-03-07
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
CPC classification number: B01D11/0223 , B01D11/0242 , B01D11/0253 , B01D21/0045 , B01D21/245
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
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公开(公告)号：US09931584B2
公开(公告)日：2018-04-03
申请号：US15010890
申请日：2016-01-29
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
CPC classification number: B01D11/0223 , B01D11/0242 , B01D11/0253 , B01D21/0045 , B01D21/245
Abstract: This disclosure describes systems, methods, and apparatus for counter-current solids leaching. A multi-stage countercurrent leaching chamber can include a top and bottom end, a barren liquor input, two or more regions for countercurrent mixing, and a barren solids output. The input can be configured to receive barren liquor. The two or more regions for countercurrent mixing and separation can be configured to mix and separate liquid and solid phases. The barren solids output can be configured to collect and discharge barren solids from the bottom end of the multi-stage countercurrent leaching chamber. A fluidized bed chamber and clarifier chamber can also be included, where the fluidized bed receives a fluidizable slurry of pregnant solids and the clarifier chamber aids in separating liquids from solids passing from a top of the fluidized bed chamber to the top end of the multi-stage countercurrent leaching chamber.
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10.发明申请公开(公告)号：US20140291247A1
公开(公告)日：2014-10-02
申请号：US14219951
申请日：2014-03-19
Applicant: Drake Water Technologies, Inc.
Inventor： Ronald N. Drake
IPC: C02F1/42
CPC classification number: C02F1/42 , B01D15/02 , B01J47/10 , B01J47/14 , B01J49/10 , B01J49/12 , B01J49/14 , B01J49/85 , C02F2001/422 , C02F2001/425 , C02F2209/005 , C02F2209/006 , C02F2209/03 , C02F2209/05 , C02F2209/06 , C02F2209/40 , C02F2303/16
Abstract: Methods and apparatus for removing contaminants from liquid using a continuously circulating stream of purifying media are disclosed. In one embodiment the method includes mixing a regenerated purifying media with a contaminated liquid containing diverse contaminants; co-currently transporting the purifying media and the contaminated liquid in a mixed state; removing, using the purifying media, while co-currently transporting the purifying media and the contaminated liquid, contaminants from the contaminated liquid so as to produce a mixture of a decontaminated liquid and a contaminated purifying media; and separating contaminated purifying media from the decontaminated liquid. In addition, the contaminated purifying media is contacted in counter current fashion with a regenerant solution so as to produce a regenerated purifying media and the regenerated purifying media is returned to the mixing step, whereby the continuously circulating purifying media selectively removes contaminants from the liquid.
Abstract translation: 公开了使用连续循环的净化介质流从液体中除去污染物的方法和装置。 在一个实施方案中，该方法包括将再生的纯化介质与含有不同污染物的污染液体混合; 共同输送混合状态的净化介质和污染液体; 在同时传送净化介质和污染液体的同时，使用净化介质去除污染液体中的污染物，以产生净化液体和被污染的净化介质的混合物; 并将污染的净化介质与去污液体分离。 此外，将污染的净化介质与现有的再生剂溶液接触，以便产生再生的净化介质，并将再生的纯化介质返回到混合步骤，由此连续循环的净化介质选择性地从液体中除去污染物。
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