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    • 1. 发明授权
    • Anaerobic film biogas digester system
    • 厌氧膜沼气池系统
    • US06783677B1
    • 2004-08-31
    • US10361514
    • 2003-02-06
    • Mayyar F. Irani
    • Mayyar F. Irani
    • C02F328
    • C02F3/286C02F2301/106C12M21/04C12M23/34C12M23/36C12M23/38C12M23/58C12M25/00C12M29/18C12M41/12Y02E50/343
    • An anaerobic digester for digesting a slurry of organic waste comprising: a tank having an outer side wall and a lower inner wall, a first radiant heating floor between the outer wall and a first side of the inner wall forming a first chamber and a second radiant heating floor between the outer wall and a second and opposite side of the inner wall forming a second chamber, an inlet pipe for delivering the slurry to a lower portion of the first chamber and a outlet pipe for removing digested slurry from a lower portion of the second chamber, the slurry maintained at a depth that is greater than a height of the inner wall; and a gas collection chamber sealed to the tank along the length of the upper surface of the outer wall.
    • 1.一种用于消化有机废弃物的废水的厌氧消化器,包括:具有外侧壁和下部内壁的罐,在所述外壁与所述内壁的第一侧之间的第一辐射加热地板,形成第一室和第二辐射 形成第二室的内壁和内壁的第二和相对侧之间的加热地板,用于将浆料输送到第一室的下部的入口管和用于从第一室的下部去除消化的浆料的出口管 第二室,浆料保持在比内壁高度大的深度; 以及沿着外壁的上表面的长度密封到罐的气体收集室。
    • 3. 发明授权
    • Vacuum retort anaerobic digestion (VRAD) system and process
    • 真空蒸煮厌氧消化(VRAD)系统及工艺
    • US06632362B2
    • 2003-10-14
    • US09766140
    • 2001-01-19
    • Herman P. Miller, III
    • Herman P. Miller, III
    • C02F328
    • C02F3/28C02F1/66C02F2301/063Y02E50/343
    • This invention pertains generally to anaerobic digesters, and more particularly to a system and process that extends the range of acceptable biomass feedstock concentrations and provides pH process control of all known digestion processes: by the creation of a vacuum or vacuum retort in or before the digester that essentially acts to boil off excess liquid, thickening the liquor of the digester to an optimum value; and to control the pH of the various phases or stages of digestion by separating the component products of digestion and mixing or diffusing a portion of said component products into the mixing system of each phase of the process. A system and process: that produces a potable water effluent, clean commercially useful by-products, zero environmental emissions, a very positive ecological impact; and, that has the capability of being completely self powered plus providing energy back to the community or industry that supports or owns it.
    • 本发明一般涉及厌氧消化器,更具体地涉及延伸可接受的生物质原料浓度范围并提供所有已知消化过程的pH过程控制的系统和方法:通过在蒸煮器之前或之前产生真空或真空蒸煮 其基本上起到煮沸多余液体的作用,使蒸煮器的液体增稠至最佳值; 并且通过分离消化和混合或将一部分所述组分产物的一部分分散到该方法的每个相的混合系统中来控制消化的各个阶段或多个阶段的pH。 一个系统和过程:产生饮用水流出物,清洁商业上有用的副产物,零环境排放,非常积极的生态影响; 并且具有完全自主的能力,并提供能量回馈给支持或拥有它的社区或行业。
    • 4. 发明授权
    • Enhanced biogas production from nitrogen bearing feed stocks
    • 增加含氮原料的沼气生产
    • US06391203B1
    • 2002-05-21
    • US09721500
    • 2000-11-22
    • Alexander G. Fassbender
    • Alexander G. Fassbender
    • C02F328
    • C02F3/2846C02F1/20C02F3/286C02F2101/16C02F2301/106C12M21/04C12M23/34C12M23/36C12M27/20C12M29/02C12M47/10Y02E50/343Y10S210/903
    • A system is disclosed comprising a first anaerobic digester, an ammonia recovery vessel, and a second anaerobic digester. Microorganisms within the first anaerobic digester are primarily hydrolyzers and acetogens, and microorganisms within the second anaerobic digester are primarily methanogens. A nitrogen containing feed stock is passed to the first digester in which the feed stock is treated to accomplish hydrolysis and acetogenesis. An effluent stream from the first digester is passed to the ammonia recovery vessel in which ammonia is removed to generate a low ammonia effluent stream. The low ammonia effluent stream is then passed to the second digester in which it is treated to accomplish methanogenesis, thereby generating a biogas. In an alternate embodiment, a single anaerobic digester is used, an effluent stream is removed from the reactor, treated for ammonia removal, and recycled to the digester at a rate sufficient to keep ammonia levels within the digester sufficiently low to avoid ammonia inhibition problems. The systems may be operated under mesophilic or thermophilic conditions.
    • 公开了一种包括第一厌氧消化器,氨回收容器和第二厌氧消化器的系统。 第一厌氧消化器内的微生物主要是水解器和乙酰菌,第二厌氧消化器内的微生物主要是产甲烷菌。 将含氮原料通入第一消化器,其中处理原料以实现水解和乙酰化。 来自第一消化器的流出物流被送到氨回收容器中,其中氨被除去以产生低氨流出物流。 然后将低氨流出物流传送到第二消化器,在其中处理它们以进行甲烷生成,从而产生沼气。 在另一个实施方案中,使用单一厌氧消化器,从反应器中除去流出物流,处理氨去除,并以足以使消化器内的氨水平保持足够低以避免氨抑制问题再循环至消化器。 系统可以在嗜温或嗜热条件下操作。
    • 8. 发明授权
    • Engineered in situ anaerobic reactive zones
    • 工程原位无氧反应区
    • US06632364B1
    • 2003-10-14
    • US09877948
    • 2001-06-08
    • Suthan S. Suthersan
    • Suthan S. Suthersan
    • C02F328
    • C02F3/306B09C1/002B09C1/10B09C2101/00C02F2101/20C02F2101/322C02F2101/36Y10S210/903Y10S210/908Y10S210/912Y10S210/913
    • An in situ method and system for reductive dechlorination, the precipitation of chromium, the precipitation of heavy metals, and microbial denitrification. The invention comprises the formation of in situ anaerobic reactive zones to precipitate and filter out dissolved heavy metals as metallic sulfides, to degrade nitrate to nitrogen gas, to reduce chlorinated hydrocarbons to ethene, and to precipitate and filter out chromium. The invention is comprised of an injection well or wells that extend into a contaminated groundwater. A conduit located within the injection well conveys a reagent to the contaminated groundwater. The reagent may be a carbohydrate rich solution. Microbes digest the carbohydrates to produce sulfate reducing and methanogenic conditions within the reactive zone that include a dissolved oxygen level less than about 0.5 mg/l, a redox potential less than about −250 mv, and a dissolved organic carbon to contaminant ratio of greater than about 50:1. These biogeochemical conditions lead to the reduction of PCE to TCE to DCE to VC and eventually to ethene. These biogeochemical conditions also lead to the precipitation of heavy metals, the precipitation of chromium, and microbial denitrification.
    • 还原脱氯,铬沉淀,重金属沉淀和微生物脱氮的原位方法和系统。 本发明包括形成原位厌氧反应区,以沉淀和过滤作为金属硫化物的溶解重金属,将硝酸盐降解为氮气,将氯代烃还原成乙烯,并沉淀并过滤出铬。 本发明包括注入井或延伸到污染地下水中的井。 位于注射井内的导管将试剂输送到污染的地下水。试剂可以是富含碳水化合物的溶液。 微生物消化碳水化合物以在反应性区域内产生硫酸盐还原和产甲烷条件,其包括小于约0.5mg / l的溶解氧水平,小于约-250mv的氧化还原电位,以及溶解的有机碳与污染物的比例大于 约50:1。 这些生物地球化学条件导致PCE对TCE的减少到DCE到VC,最终还原为乙烯。 这些生物地球化学条件也导致重金属沉淀,铬沉淀和微生物脱氮。
    • 9. 发明授权
    • Method and device for anaerobic purification of waste water using the UASB method
    • 使用UASB方法对废水进行厌氧净化的方法和装置
    • US06478963B1
    • 2002-11-12
    • US09647944
    • 2000-12-27
    • Peter Rossmanith
    • Peter Rossmanith
    • C02F328
    • C02F3/2873C02F3/2846
    • Described is a method and a device for purifying waste water, in particular by means of anaerobic purification. The method is carried out in a waste water- and sludge-receiving container under generation of gas, the developing gas being trapped by a gas collector and the circulation formed by the ascending gas being used for loosening the sludge which has settled on the bottom of the container. Such a method is to be developed in a constructionally simple and more efficient way. To this end the settled sludge should be sucked from the bottom by a gas lifting effect provided by the ascending gas, and should be passed into the upper portion of the container in a condition separated from the waster water in the container, and returned into the waste water.
    • 描述了用于净化废水的方法和装置,特别是通过厌氧净化。 该方法在产生气体的废水和污泥收集容器中进行,显影气体被气体收集器捕获,并且由上升气体形成的循环用于松动沉积在底部的污泥 容器 这种方法将以结构简单和更有效的方式开发。 为此,沉淀的污泥应通过由上升气体提供的气举效应从底部吸入,并以与容器中的废水分离的状态进入容器的上部,并返回到 废水。