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公开(公告)号：US06984323B2
公开(公告)日：2006-01-10
申请号：US10010271
申请日：2001-11-05
申请人： Boris M. Khudenko
发明人： Boris M. Khudenko
IPC分类号： C02F3/30
CPC分类号： C12M27/24 , C02F1/20 , C02F3/282 , C02F3/301 , C12M21/04 , C12M23/34 , C12M29/08 , Y02E50/343 , Y10S210/903 , Y10S210/906
摘要： This is a method of waste treatment in tall reactors having with anaerobic biological stage in the lower section of the reactor and another treatment stage in the upper section of the reactor, these stages are separated by an essentially horizontal partition. Presurized digestion gases generated in the anaerobic section are collected under the partition. The process is further improved by providing a recuperable alkalinity and stripping of biologically generated carbon dioxide. so that the free carbon dioxide concentratioon in the anaerobic mixed liquor is very low and a methane-rich digestion gas is produced. Production of pressurized methane-rich digestion gas is the major benefit of the process. Ather improvements are in the controllable gaslift mixing with gases other than digestion gases, improved process performance with increasing operating temperatures due to bioheating, and improved solid-liquid separation due to the use of the distillation techniques making use of the bioheating and heat recycle.
摘要翻译： 这是在反应器的下部具有厌氧生物阶段的高反应器中的废物处理方法，并且在反应器上部的另一个处理阶段，这些阶段被基本上水平的分隔开。 在厌氧部分产生的预先消化的气体被收集在隔板下面。 通过提供可恢复的碱度和生物生成的二氧化碳的汽提来进一步改进该方法。 使得厌氧混合液中的游离二氧化碳浓度非常低，并且产生富含甲烷的消化气体。 加压甲烷富集消化气的生产是该方法的主要优点。 其他改进在与消化气体以外的气体的可控气体提升混合中，由于使用生物加热和热循环利用蒸馏技术，由于生物加热而改进的工艺性能以及由于生物加热引起的操作温度升高以及改进的固液分离。
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公开(公告)号：US20090045135A1
公开(公告)日：2009-02-19
申请号：US11893872
申请日：2007-08-18
CPC分类号： C02F1/444 , B01D2311/04 , C02F1/004 , C02F3/06 , C02F2303/16 , Y02W10/15 , B01D2311/2649
摘要： This is a method of filtration of a liquid comprising steps of sequential filtration of said liquid through at least one deep bed medium producing at least one first filtrate followed by at least one membrane medium filtration producing at least one second filtrate, wherein said membrane medium is at least periodically within said deep bed media Many types of deep bed and membrane media can be used. The domain of using contact clarification (direct filtration) can be expanded towards greater solids concentration. Operation and backwash, is simplified, continuous filtration becomes possible. Water can be water from natural source water, process water, wastewater, aqueous or non-aqueous suspensions, emulsions, solutions. Treatment can include mechanical interception of suspended particles, chemical, physical chemical, electrochemical, and biological processes. In water and wastewater processing, control over suspended solids, BOD, COD, nitrogen and phosphorus compounds, bacteria and viruses, heavy metals, color, and other constituents can be dramatically improved as compared to conventional processes. The method can be accommodated in new and modified existing treatment systems.
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公开(公告)号：US5616241A
公开(公告)日：1997-04-01
申请号：US532606
申请日：1995-10-12
申请人： Boris M. Khudenko
发明人： Boris M. Khudenko
CPC分类号： C02F3/1221 , C02F3/006 , C02F3/28 , C02F3/2806 , C02F3/30 , C02F3/302 , C02F3/308 , C02F2209/02 , C02F2209/06 , C02F2209/08 , C02F2209/20 , C02F2209/22 , C02F2209/245 , C02F2209/28 , C02F2209/38 , C02F2209/40 , C02F2307/08 , Y02E50/343 , Y02W10/15
摘要： A system for treatment of influent materials such as wastewater, gases, solid and liquid waste, and sludges utilizes an anaerobic reactor followed by at least one sludge separator and at least one sludge conditioner. In the sludge conditioner, anaerobic and aerobic biological actions, chemical or other treatment methods are applied to produce the optimal make-up of the conditioned sludge in the system overall. Single channel or multiple channel conditioners are possible. In such a system controllable cultivation and use, and controllable conversion of constituents in said influent materials are provided. The method of controllable anaerobic treatment is illustrated as a stand-alone anaerobic treatment, coupled anaerobic/aerobic treatment, combined anaerobic/aerobic treatment, treatment of wastewater within collection networks, treatment of wastewater sludges, and treatment of gases. The aerobic reactor can be stacked on top of the anaerobic reactor, with optional gas collection above the aerobic reactor.
摘要翻译： PCT No.PCT / US94 / 03374 Sec。 371 1995年10月12日第 102（e）日期1995年10月12日PCT 1994年3月28日PCT公布。 出版物WO94 / 24056 日期1994年10月27日废水，气体，固体废物和废液等污水处理系统和污泥利用厌氧反应器，随后至少有一个污泥分离器和至少一个污泥调节剂。 在污泥调节剂中，应用厌氧和需氧生物作用，采用化学或其他处理方法，在系统中整体生产调理污泥的最佳组成。 单通道或多通道调节器是可能的。 在这种系统中可控制的培养和使用，并且提供了所述流入物质中成分的可控转化。 可控厌氧处理的方法被描述为独立的厌氧处理，联合厌氧/需氧处理，联合厌氧/需氧处理，收集网络中的废水处理，废水污泥的处理和处理气体。 好氧反应器可以堆放在厌氧反应器的顶部，可选的气体收集在需氧反应器之上。
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公开(公告)号：US5514277A
公开(公告)日：1996-05-07
申请号：US102618
申请日：1993-08-05
申请人： Boris M. Khudenko
发明人： Boris M. Khudenko
CPC分类号： C02F3/1221 , C02F3/006 , C02F3/28 , C02F3/2806 , C02F3/302 , C02F3/308 , C02F2209/02 , C02F2209/06 , C02F2209/08 , C02F2209/20 , C02F2209/22 , C02F2209/245 , C02F2209/28 , C02F2209/38 , C02F2209/40 , C02F3/30 , Y02E50/343 , Y02W10/15
摘要： A system for wastewater and sludge treatment utilizes an anaerobic reactor to modify the wastewater and generate sludge and liquid effluent. The sludge is transferred to a conditioner wherein anaerobic, aerobic and chemical means may be utilized to cultivate the required strains of organisms and break down various pollutants. Various chemicals may be solubilized, or precipitated, or adsorbed to remove them from the waste stream. Aerobic conditioning may be used to increase the volume of sludge, and to increase the temperature of the sludge. A shell having multiple compartments can provide for the entire process by utilizing the upper portion for anaerobic reaction and the lower portion for conditioning. An aerobic reactor can be disposed centrally of the conditioning compartments. Pipes and pumps can be used to transfer components from one compartment to another, and to discharge the cleaned effluent. The sludge is further subjected to aerobic reaction and bioheating. Some chemicals may be added to assist in removal of heavy metals and other toxic substances. Finally, the sludge and water are separated, and the sludge is dried.
摘要翻译： 废水和污泥处理系统利用厌氧反应器改造废水，产生污泥和液体流出物。 将污泥转移到调理剂中，其中可以利用厌氧，需氧和化学方法培养所需的生物菌株并分解各种污染物。 各种化学物质可能溶解，沉淀或吸附，以将其从废物流中除去。 有氧条件可用于增加污泥的体积，并增加污泥的温度。 具有多个隔室的壳体可以通过利用上部的厌氧反应和下部的调理来提供整个过程。 需氧反应器可以设置在调节室的中央。 管道和泵可用于将组件从一个隔间传输到另一个隔室，并排出清洁的污水。 污泥进一步进行好氧反应和生物加热。 可添加一些化学物质来帮助去除重金属和其他有毒物质。 最后，污泥和水分离，污泥干燥。
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公开(公告)号：USRE34298E
公开(公告)日：1993-06-29
申请号：US751864
申请日：1991-08-28
CPC分类号： F23G5/008 , F23G5/16 , F23G5/50 , F23G2207/101 , F23G2207/102 , F23G2207/20 , F23G2207/30 , F23G2207/40 , F23G2900/50007 , F23G2900/55002 , F23G2900/55006 , F23G2900/55007 , F23L2900/07005 , F23N2005/181 , F23N2005/185 , F23N2021/12 , F23N2025/04 , F23N2025/06 , F23N2025/10 , F23N2037/28 , F23N2037/32 , F23N5/003 , F23N5/08 , Y02E20/344
摘要： The invention relates to an afterburner apparatus and an incineration system and methods of waste destruction in primary incineration combustion means and afterburner means which both preferably utilize at least two different oxidizing gases. By varying the ratio of said oxidizing gases, the amount of total oxygen and nitrogen delivered in either means can be dynamically adjusted in accordance with the process requirements. Varying the flows of at least two oxydizing gases and auxiliary fuel in both the primary incinerator and afterburner makes it possible to operate the system under fluctuating waste loading conditions, by controlling temperature, partial pressure of oxygen and heat available for the process as a function of said ratio.
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公开(公告)号：US4861262A
公开(公告)日：1989-08-29
申请号：US9145
申请日：1987-01-29
IPC分类号： B05B7/08 , C21C5/46 , F23G5/16 , F23G5/32 , F23G5/50 , F23G7/06 , F23L7/00 , F23M5/08 , F23N5/00 , F23N5/08 , F23N5/18
CPC分类号： B05B7/0861 , C21C5/4606 , F23G5/16 , F23G5/32 , F23G5/50 , F23G7/065 , F23L7/00 , F23M5/08 , F23G2207/101 , F23G2207/102 , F23G2207/20 , F23G2207/30 , F23G2207/40 , F23G2900/50007 , F23G2900/55002 , F23G2900/55006 , F23G2900/55007 , F23L2900/07005 , F23N2005/181 , F23N2005/185 , F23N2021/12 , F23N2025/04 , F23N2025/06 , F23N2025/10 , F23N2037/28 , F23N2037/32 , F23N5/003 , F23N5/08 , Y02E20/344 , Y02P10/34
摘要： The invention relates to an afterburner apparatus and an incineration system and methods of waste destruction in primary incineration combustion means and afterburner means which both preferably utilize at least two different oxidizing gases. By varying the ratio of said oxidizing gases, the amount of total oxygen and nitrogen delivered in either means can be dynamically adjusted in accordance with the process requirements. Varying the flows of at least two oxydizing gases and auxiliary fuel in both the primary incinerator and afterburner makes it possible to operate the system under fluctuating waste loading conditions, by controlling temperature, partial pressure of oxygen and heat available for the process as a function of said ratio.
摘要翻译： 本发明涉及一种后燃器装置和一种焚烧系统以及主要焚烧燃烧装置和后燃器装置中废物破坏的方法，它们优选利用至少两种不同的氧化气体。 通过改变所述氧化气体的比例，可以根据工艺要求动态地调节在任一装置中输送的总氧气和氮气的量。 在主要焚烧炉和加力燃烧器中，改变至少两种氧化气体和辅助燃料的流动使得可以通过控制温度，氧气分压和过程可用的热量作为功能，在波动的废物负载条件下操作系统 说比例。
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公开(公告)号：US4713102A
公开(公告)日：1987-12-15
申请号：US897326
申请日：1986-08-18
申请人： Boris M. Khudenko , Jack Zbar
发明人： Boris M. Khudenko , Jack Zbar
CPC分类号： B01D9/0009
摘要： A method and apparatus for concentrating multicomponent liquid product containing volatile and nonvolatile constituents are provided, comprising mixing liquid product with liquid refrigerant gas in a freezing chamber, removing ice crystals containing entrained multicomponent liquid product from the chamber, removing the volatile constituents of the liquid product and vaporized liquid refrigerant gas from the chamber, separating the volatile constituents and vaporized refrigerant gas, recirculating the volatile constituents into the freezing chamber so as to mix with the remaining liquid product in the chamber, and removing concentrate of the liquid product from the chamber.
摘要翻译： 提供了一种用于浓缩含有挥发性和不挥发成分的多组分液体产物的方法和装置，包括将液体产物与液体制冷剂气体在冷冻室中混合，从室中除去含有夹带的多组分液体产物的冰晶，除去液体产物的挥发性成分 从室中汽化液体制冷剂气体，分离挥发性成分和蒸发的制冷剂气体，将挥发性成分再循环到冷冻室中，以与室中的剩余液体产物混合，并从室中除去液体产物的浓缩物。
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公开(公告)号：US07553418B2
公开(公告)日：2009-06-30
申请号：US11893872
申请日：2007-08-18
IPC分类号： C02F3/00
CPC分类号： C02F1/444 , B01D2311/04 , C02F1/004 , C02F3/06 , C02F2303/16 , Y02W10/15 , B01D2311/2649
摘要： This is a method of filtration of a liquid comprising steps of sequential filtration of said liquid through at least one deep bed medium producing at least one first filtrate followed by at least one membrane medium filtration producing at least one second filtrate, wherein said membrane medium is at least periodically within said deep bed media Many types of deep bed and membrane media can be used. The domain of using contact clarification (direct filtration) can be expanded towards greater solids concentration. Operation and backwash, is simplified, continuous filtration becomes possible. Water can be water from natural source water, process water, wastewater, aqueous or non-aqueous suspensions, emulsions, solutions. Treatment can include mechanical interception of suspended particles, chemical, physical chemical, electrochemical, and biological processes. In water and wastewater processing, control over suspended solids, BOD, COD, nitrogen and phosphorus compounds, bacteria and viruses, heavy metals, color, and other constituents can be dramatically improved as compared to conventional processes. The method can be accommodated in new and modified existing treatment systems.
摘要翻译： 这是一种过滤液体的方法，包括以下步骤：通过至少一个深床介质顺序过滤所述液体，产生至少一个第一滤液，随后至少一个膜介质过滤产生至少一个第二滤液，其中所述膜介质是 至少周期性地在所述深床介质中可以使用许多类型的深床和膜介质。 使用接触澄清（直接过滤）的领域可以扩大到更大的固体浓度。 操作和回洗，简化，连续过滤成为可能。 水可以是天然来源水，工艺用水，废水，水性或非水悬浮液，乳液，溶液的水。 处理可以包括机械拦截悬浮颗粒，化学，物理化学，电化学和生物过程。 在水和废水处理中，与常规方法相比，可以显着改善对悬浮固体，BOD，COD，氮和磷化合物，细菌和病毒，重金属，颜色和其他成分的控制。 该方法可以适应新的和改进的现有治疗系统。
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公开(公告)号：US5348629A
公开(公告)日：1994-09-20
申请号：US650936
申请日：1991-02-05
申请人： Boris M. Khudenko
发明人： Boris M. Khudenko
CPC分类号： C02F1/46176 , G21B3/00 , C02F1/463 , C02F1/467 , Y02E30/18
摘要： A method and apparatus for the electrochemical processing of materials in which the material to be processed is located within an electrolyte that is subjected to strong local electromagnetic fields in a migrational transport layer, causing strong electromagnetic and electrokinetic forces capable of effecting the chemical and physical conversions in the materials to be processed. This migrational transport layer can be induced either by creating a cementation system, applying an outside source of current to an electrode system, or a combination of both.
摘要翻译： 一种用于电化学处理材料的方法和装置，其中待处理的材料位于在迁移运输层中经受强的局部电磁场的电解质中，导致能够实现化学和物理转化的强电磁和电动力 在待处理的材料中。 这种迁移传输层可以通过产生胶结系统，向电极系统施加外部电流源或两者的组合来诱导。
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公开(公告)号：US4472358A
公开(公告)日：1984-09-18
申请号：US382615
申请日：1982-05-27
申请人： Boris M. Khudenko
发明人： Boris M. Khudenko
CPC分类号： B01J19/32 , B01J8/34 , B01J2219/32231 , B01J2219/32248 , Y10S261/72
摘要： Packing for fluidized bed reactors, is improved by providing alternately inclined baffles connected directly to each other or by means for connecting the said baffles into grids located in one or several levels, the said baffles forming expanding and contracting cells in the direction of the flow. The size, spacing in grids and the angle of attack of these baffles and spacing of grids are the same throughout the reactor volume when uniform distributions of the fluidizing agent and the fluidized medium are required. Alternatively, a device of this type is improved by providing variable sizes, spacing in grids, and angle of attack of these baffles and spacing of grids when specified nonuniform distributions of the flow of the fluidizing agent and the concentrations of the fluidized media are desired for particular applications.
摘要翻译： 用于流化床反应器的包装通过提供彼此直接连接的交替倾斜的挡板或通过将所述挡板连接到位于一个或多个水平的网格的装置来改进，所述挡板在流动方向上形成扩张和收缩的单元。 当需要流化剂和流化介质的均匀分布时，这些挡板的尺寸，间距以及这些挡板的迎角和格栅的间距在整个反应器体积中是相同的。 或者，通过提供可变尺寸，网格间距和这些挡板的迎角以及当流化剂流的特定不均匀分布和流化介质的浓度期望格栅的间距时，可以改善这种装置， 特殊应用。
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