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公开(公告)号:US10479704B2
公开(公告)日:2019-11-19
申请号:US15908525
申请日:2018-02-28
发明人: Missy Hayes , Gina Sacco , Nancy S. Sherwood
IPC分类号: C02F1/28 , C09K8/536 , C09K8/80 , B01D15/08 , B01D53/02 , C09K8/52 , C02F101/10 , C02F101/14 , C02F101/18 , C02F101/20 , C02F103/10
摘要: The invention relates to the proppants and proppant substrates treated with active compounds that reduce the presence of contaminants in fluids, methods of using those materials, as well as methods of making those materials. The invention further provides that the contaminated fluids are associated with wells, including oil and gas wells.
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公开(公告)号:US20170305769A1
公开(公告)日:2017-10-26
申请号:US15643710
申请日:2017-07-07
发明人: John T. Groves , Thomas P. Umile
IPC分类号: C02F1/76 , C02F1/72 , B01J31/18 , C02F101/18
CPC分类号: C02F1/76 , B01J31/1815 , B01J2231/70 , B01J2531/025 , B01J2531/72 , C02F1/725 , C02F2101/18 , C02F2305/023
摘要: Methods, kits, cartridges, and compounds related to generating chlorine dioxide by exposing ClO2− to at least one of a manganese porphyrin catalyst or a manganese porphyrazine catalyst are described. Methods, kits, cartridges, and compounds related to decomposed cyanide ions and hydrogen cyanide for water decontamination.
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公开(公告)号:US09464368B2
公开(公告)日:2016-10-11
申请号:US12918372
申请日:2009-02-12
申请人: Eyal Zussman , Yael Dror , Jonathan Charles Kuhn
发明人: Eyal Zussman , Yael Dror , Jonathan Charles Kuhn
IPC分类号: D01D5/24 , D01F1/08 , A61K9/00 , D01D5/00 , B82Y30/00 , C02F3/10 , C02F3/34 , D01D5/247 , D01F1/10 , D01F8/14 , G01N33/543 , C02F101/18 , C02F101/20 , C02F101/30 , C02F101/36
CPC分类号: C12N11/04 , A61K9/0092 , A61K38/44 , B82Y30/00 , C02F3/102 , C02F3/34 , C02F3/342 , C02F2101/18 , C02F2101/20 , C02F2101/306 , C02F2101/36 , C02F2305/08 , C09D167/04 , C09D171/02 , C12M21/18 , C12M23/06 , C12M23/16 , C12Q1/66 , C12Y113/12007 , C12Y114/16001 , D01D5/003 , D01D5/247 , D01F1/10 , D01F8/14 , G01N33/54393 , G01N2333/90241 , Y02W10/15 , Y10T428/1393
摘要: Provided is a method of attaching a molecule-of-interest to a microtube, by co-electrospinning two polymeric solutions through co-axial capillaries, wherein a first polymeric solution of the two polymeric solutions is for forming a shell of the microtube and a second polymeric solution of the two polymeric solutions is for forming a coat over an internal surface of the shell, the first polymeric solution is selected solidifying faster than the second polymeric solution and a solvent of the second polymeric solution is selected incapable of dissolving the first polymeric solution and wherein the second polymeric solution comprises the molecule-of-interest, thereby attaching the molecule-of-interest to the microtube. Also provided is an electrospun microtube comprising an electrospun shell, an electrospun coat over an internal surface of the shell and a molecule-of-interest attached to the microtube.
摘要翻译: 提供了通过共同静电纺丝两个聚合物溶液通过同轴毛细管将感兴趣分子附着到微管的方法,其中两个聚合物溶液的第一聚合溶液用于形成微管的壳,第二聚合溶液用于形成微管 两种聚合物溶液的聚合物溶液用于在壳的内表面上形成涂层,选择第一聚合物溶液比第二聚合物溶液更快地固化,并且选择第二聚合物溶液的溶剂不能溶解第一聚合物溶液 并且其中所述第二聚合物溶液包含感兴趣的分子,从而将感兴趣的分子附着到微管。 还提供了一种电纺微管,其包括电纺壳,在壳的内表面上的电纺丝涂层和附着于微管的感兴趣分子。
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公开(公告)号:US20120061316A1
公开(公告)日:2012-03-15
申请号:US13321669
申请日:2010-08-26
IPC分类号: C02F3/12 , C02F101/18 , C02F103/00 , C02F101/34
CPC分类号: C02F3/12 , C02F3/006 , C02F3/341 , C02F2101/101 , C02F2101/16 , C02F2101/18 , C02F2101/345 , C02F2101/38 , C02F2101/40 , C02F2103/18 , C02F2209/08 , C02F2209/36 , Y02W10/15
摘要: The present invention provides a biological treatment method of biologically treating the subject water containing phenol, thiocyanate and the like, which improves the quality of treated water, while suppressing a reduction in treatment efficiency. As a means for achieving the aforementioned object, the present invention relates to a biological treatment method including introducing subject water containing a COD component, wherein the COD component is at least one of phenol and thiocyanate, into a biological treatment tank containing sludge containing bacteria capable of decomposing the COD component to thereby biologically treat the COD component with the bacteria, wherein, before the introduction of the subject water into the biological treatment tank, a step of counting the total number of bacteria contained in the sludge is carried out, so that the amount of the COD component loaded on a single bacterium per unit time can be controlled within a predetermined range.
摘要翻译: 本发明提供一种生物处理含有苯酚,硫氰酸盐等的目标水的生物处理方法,其提高了处理水的质量,同时抑制了处理效率的降低。 作为实现上述目的的手段,本发明涉及一种生物处理方法,其包括将含有COD成分的目标水(其中COD成分为苯酚和硫氰酸盐中的至少一种)引入含有含细菌污泥的生物处理槽中的生物处理方法 分解COD成分,由此用细菌对COD成分进行生物处理,其中,在将被摄体的水引入生物处理槽之前,进行计数污泥中所含细菌总数的步骤,使得 每单位时间装载在单个细菌上的COD成分的量可以控制在预定范围内。
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公开(公告)号:US07897049B2
公开(公告)日:2011-03-01
申请号:US11749448
申请日:2007-05-16
申请人: Rajat S. Ghosh , Dennis Fulmer , Kevin Kitzman , John Smith
发明人: Rajat S. Ghosh , Dennis Fulmer , Kevin Kitzman , John Smith
IPC分类号: C02F1/62 , C02F1/70 , C02F101/18 , C02F101/22
CPC分类号: C02F1/705 , C02F1/283 , C02F1/286 , C02F2101/103 , C02F2101/18 , C02F2101/22 , C02F2103/16 , C02F2209/04 , Y10S210/904 , Y10S210/911 , Y10S210/912 , Y10S210/913
摘要: Systems and associated methods for treating contaminant-containing wastewater are provided. The systems generally include a reducing zone for reducing the oxidation-reduction potential of the water and a clean-up zone comprising zero valent iron for removing at least a portion of the contaminant from the contaminant-containing water. The systems are operable to remove one or more contaminants from the contaminant-containing water and are operable for extended durations without clogging due to the formation of iron hydroxides.
摘要翻译: 提供了处理含污染废水的系统和相关方法。 该系统通常包括用于降低水的氧化还原电位的还原区和包含用于从含污染物的水中去除至少一部分污染物的零价铁的净化区。 该系统可操作以从含污染物的水中除去一种或多种污染物,并且由于氢氧化铁的形成而可延长持续时间而不堵塞。
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公开(公告)号:US12116295B2
公开(公告)日:2024-10-15
申请号:US17269852
申请日:2019-08-09
IPC分类号: C02F1/76 , C02F1/72 , B01J23/755 , C02F101/18
CPC分类号: C02F1/725 , C02F1/722 , C02F1/76 , B01J23/755 , C02F2101/18 , C02F2209/06
摘要: There are provided systems (10) and processes for the selective removal of cyanide from a wastewater stream (12) comprising cyanide and an amount of organic compounds therein.
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公开(公告)号:US11760675B2
公开(公告)日:2023-09-19
申请号:US18193685
申请日:2023-03-31
发明人: Mu Liu , Zehua Li , Huiming Han , Xiaofeng Lin , Yingqiang Su , Mengyuan Duan , Cong Xiao , Kai Sun , XiKun Zhu
IPC分类号: C02F9/00 , C02F1/52 , C02F1/62 , C02F1/72 , C02F3/30 , C02F1/58 , C02F101/18 , C02F101/20 , C02F103/34
CPC分类号: C02F9/00 , C02F1/52 , C02F1/586 , C02F1/62 , C02F1/725 , C02F3/30 , C02F2101/18 , C02F2101/20 , C02F2103/346 , C02F2209/06 , C02F2209/08
摘要: A system for treating printed circuit board wastewater (PCB) includes a production system, a pretreatment system, a biochemical system, a recovery system and a concentrated water treatment system. The production system is configured for producing process water and auxiliary water from tap water. The pretreatment system is configured to pretreat different wastewater samples separately. The biochemical system is configured to decompose the pretreated wastewater. The recovery system is configured to treat wastewater from the pretreatment system and the biochemical system to obtain process water and feed concentrated water to the concentrated water treatment system. The concentrated water treatment system is configured to treat the concentrated water to meet a discharge standard. A treatment method for the PCB wastewater is also provided.
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公开(公告)号:US11685681B2
公开(公告)日:2023-06-27
申请号:US17409554
申请日:2021-08-23
发明人: Chongwu Guo , Fonvoon Lai
IPC分类号: C02F9/00 , C02F1/52 , C02F1/00 , C02F1/28 , C02F1/66 , C02F1/70 , C02F3/02 , C02F1/56 , C02F101/18 , C02F101/38 , C02F101/34 , C02F101/22 , C02F103/16 , C02F1/72
CPC分类号: C02F9/00 , C02F1/004 , C02F1/283 , C02F1/5245 , C02F1/56 , C02F1/66 , C02F1/70 , C02F1/72 , C02F3/02 , C02F2101/18 , C02F2101/22 , C02F2101/34 , C02F2101/38 , C02F2103/16 , C02F2209/04 , C02F2209/06 , C02F2301/08
摘要: A method for treatment of mixed electroplating wastewater without a cyanide and a phosphorus-containing reductant without a cyanide and a phosphorus-containing reductant. A ferrous chloride solution is added into electroplating wastewater without a cyanide and a phosphorus-containing reductant. The pH of wastewater is adjusted to 10.5-12. Pollutants such as sodium cyanide and hydroxyl-containing organic amine complexants are oxidized with sodium hypochlorite. Carboxyl-containing organic acid complexants are precipitated. Hexavalent chromium is reduced to trivalent chromium to form chromium hydroxide precipitate. Precipitate is removed by filtering and wastewater is adjusted to pH 4.5-5.5. Heavy metal ions are precipitated with sodium dimethyldithiocarbamate or sodium diethyldithiocarbamate. Precipitate and heavy metal capturing agents are adsorbed with activated carbon followed by removal of precipitate. Wastewater is adjusted to pH 6-8. Aliphatic polyamine complexants are destroyed using an available biological degradation technique to reduce chemical oxygen demand.
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公开(公告)号:US11667553B2
公开(公告)日:2023-06-06
申请号:US16091601
申请日:2017-04-06
申请人: EISENMANN SE
发明人: Jochen Schumacher
IPC分类号: C02F1/72 , C02F1/66 , C02F101/18 , C02F103/10 , C02F103/16 , C02F103/34 , C02F103/36 , C02F103/40
CPC分类号: C02F1/722 , C02F1/66 , C02F1/725 , C02F2101/18 , C02F2103/10 , C02F2103/16 , C02F2103/343 , C02F2103/36 , C02F2103/40 , C02F2209/003 , C02F2209/02 , C02F2209/06 , C02F2301/046 , C02F2301/08
摘要: A method and system for treating cyanide-containing fluids, in particular cyanide-containing waste water, wherein cyanide-containing fluid is subject to a pretreatment in a pretreatment zone, in which at least one predetermined pH value and a predetermined temperature is set, wherein a base fluid is formed with the pretreatment. Base fluid is reacted at least with an oxidation means in at least one reaction reactor, whereby an oxidation reaction of the cyanide is initiated. Fluid from the reaction reactor is transferred as intermediate fluid into at least one process reactor, in which conditions exist in which the oxidation reaction of the cyanide initiated in the reaction reactor can take place, wherein a process fluid is formed. A continuous flow of fluid is maintained at least periodically, wherein the base fluid is transferred continuously from the pretreatment zone into the reaction reactor, intermediate fluid is transferred continuously from the reaction reactor into the process reactor, and process fluid is removed continuously from the process reactor.
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公开(公告)号:US09688606B2
公开(公告)日:2017-06-27
申请号:US15031100
申请日:2014-10-22
发明人: Samuel Neto , Rüdiger Fritz , Renate Hempel , Holger Allardt , Yuan Shen Dai , Barbara Becker , Sebastian Ahrens , Julia Leschinski , Henrich Hermann , Mirko Haendel , Jürgen Pöhlmann
IPC分类号: C07C201/16 , C07C205/06 , B01D11/04 , C02F1/20 , C02F1/26 , C02F3/00 , B01D11/00 , C02F101/18 , C02F103/36
CPC分类号: C07C201/16 , B01D11/0488 , B01D11/0492 , B01D2011/002 , C02F1/20 , C02F1/26 , C02F3/00 , C02F2101/18 , C02F2103/36 , C07C205/06
摘要: Process for scrubbing a crude mixture which is obtained in the nitration of toluene after separating off the nitrating acid and comprises dinitrotoluene, nitric acid, nitrogen oxides and sulfuric acid, which comprises two scrubbing steps (WS-I) and (WS-II), whereini) in a first scrubbing step (WS-I), the crude mixture is extracted with a scrubbing acid I comprising nitric acid, nitrogen oxides and sulfuric acid in a scrub comprising at least one extraction stage, where the scrubbing acid discharged from the first extraction stage (WS-I-1) of the first scrubbing step (WS-I) has a total acid content of from 10 to 40% by weight and a content of from 80 to 350 ppm of hydrocyanic acid, giving a prescrubbed crude mixture,ii) in a second scrubbing step (WS-II), the prescrubbed crude mixture comprising dinitrotoluene is extracted with a scrubbing acid II in a scrub comprising at least one, preferably at least 2, extraction stage(s), where the scrubbing acid discharged from the first extraction stage (WS-II-1) of the second scrubbing step (WS-II) has a pH of less than or equal to 4, giving a dinitrotoluene-comprising mixture which is essentially free of nitric acid, sulfuric acid, nitrogen oxides and hydrocyanic acid and has a content of not more than 300 ppm of nitric acid and nitrogen oxides, not more than 3 ppm of sulfate and not more than 50 ppm of hydrocyanic acid.
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