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    • 91. 发明公开
    • 부양식 슬러지 건조 장치
    • 浮动式泥浆干燥装置
    • KR1020100089231A
    • 2010-08-12
    • KR1020090008388
    • 2009-02-03
    • (주)피지티
    • 전성식
    • C02F1/40C02F11/04C02F11/12
    • C02F1/40C02F11/04C02F11/12C02F2201/002Y02W10/20
    • PURPOSE: A plurality of connection tubings and the hot-air bower and possessively used according to speed of the sewage sludge are included. The energy efficiency and drying efficiency can be enhanced. Provided is the subform sludge drying machine. CONSTITUTION: A subform sludge drying machine. With the first hopper(1) in which the sewage sludge flows in. With the hot-air bower(2) for desiccating to the air having the heat of the high temperature the sewage sludge traffic flows with the first hopper and flows in into the inside of the first hopper. It is located in the upper of the first hopper. With the second hopper(3) flowing in into the state distributed to the particle in which the sewage sludge which is connected to the first hopper and passes through the first hopper smalls.
    • 目的:包括多个连接管道和根据污水污泥速度占有用量的热空气。 提高能源效率和干燥效率。 提供亚型污泥干燥机。 构成:亚型污泥干燥机。 用污水污泥流入的第一个料斗(1),用热风(2)将干燥至高温空气的污水污泥交通流与第一个料斗一起流入 在第一个料斗的内部。 它位于第一个料斗的上部。 随着第二料斗(3)流入分配到颗粒的状态,其中连接到第一料斗并通过第一料斗的污泥污泥较小。
    • 93. 发明授权
    • 이산화탄소를 이용한 부상분리공정에 따른 오폐수처리시설 및 그 방법
    • 使用碳泡沫浮选的废水处理厂及其方法
    • KR100961464B1
    • 2010-06-09
    • KR1020090086120
    • 2009-09-11
    • 주식회사 부강테크곽동희
    • 곽동희유대환
    • C02F1/24C02F1/52C02F11/04
    • Y02E50/343C02F1/24C02F1/52C02F11/04Y02W10/20
    • PURPOSE: A waste water treatment facility and a waste water disposal method are provided to apply to a low carbon green industry by using greenhouse gas carbon dioxide, and to perform a flotation-separation process without a special saturated unit, and a pressurization unit. CONSTITUTION: A waste water treatment facility(100) comprises the following: a mixing/agglomeration section inflowing waste water and carbon dioxide, mixing and coagulating the waste water, dissolving a carbon dioxide in the waste water; a flotation separate unit(110) floating waste water by using and dividing carbon dioxide, lowering a pressure of an effluent of the mixing/agglomeration section; a carbon fixation part(150) fixing carbon dioxide. The mixing/agglomeration section changes pressure of the mixing/agglomeration section inside, and dissolves carbon dioxide into waste water through a temperature change of the mixing/agglomeration section inside and the change of injection amount of carbon dioxide flowing in the mixing/agglomeration section without a separated pressure device.
    • 目的:提供废水处理设备和废水处理方法,通过使用温室气体二氧化碳应用于低碳绿色工业,并进行无需特殊饱和单元的浮选分离过程和加压单元。 规定:废水处理设备(100)包括以下步骤:将废水和二氧化碳进入混合/聚集部分,将废水混合并凝结,将二氧化碳溶解在废水中; 浮选分离单元(110)通过使用和分解二氧化碳来浮选废水,降低混合/附聚段的流出物的压力; 固定二氧化碳的碳固定部分(150)。 混合/凝聚部分改变内部的混合/附聚部分的压力,并且通过内部的混合/附聚部分的温度变化和在混合/附聚部分中流动的二氧化碳的注入量的变化而将二氧化碳溶解到废水中,而没有 一个分离的压力装置。
    • 94. 发明公开
    • 오니 처리 시스템
    • 污水处理系统
    • KR1020100061523A
    • 2010-06-07
    • KR1020107007627
    • 2008-10-15
    • 가부시끼가이샤 도시바
    • 오바라다쿠미아시카가노부유키하라구치사토시하야미도쿠스케야마모토가츠야다무라히로시
    • C02F11/18C02F11/04
    • C02F11/18C02F11/04C02F11/12F23G7/001F23G2900/50208Y02E50/343Y02W10/23
    • Sludge can be effectively heat-treated with neither the drop of heat-treatment efficiency due to the adhesion of a sludge component to a heat transfer face nor the clogging of a passage with the sludge. The sludge is subjected to a heat-treatment by heating it by a reactor (14) under a predetermined pressure. Before this heat-treatment by the reactor (14), the sludge is preheated by a preheating device (13). This preheating device (13) is constituted by integrating a direct heat exchanger portion (15) connected to a feed passage of the sludge to the reactor (14) and an evaporator portion (16) connected to a discharge passage of the heat-treated sludge from the reactor (14). These portions are held therein at a pressure lower than that in the reactor (14). The sludge, which is introduced into the direct heat exchanger portion (15) but before heat-treated, is preheated by making direct contact with the steam which is produced from the heat-treated sludge introduced from the discharge passage into the evaporator portion (16).
    • 污泥由于污泥成分与传热面粘合而不会由于污泥的通道堵塞而能够有效地进行热处理,因此不会降低热处理效率。 通过在预定压力下通过反应器(14)加热来对污泥进行热处理。 在通过反应器(14)进行热处理之前,通过预热装置(13)预热污泥。 该预热装置(13)通过将连接到污泥的进料通道的直接热交换器部分(15)与反应器(14)和蒸发器部分(16)相结合而构成,蒸发器部分(16)连接到热处理污泥的排放通道 从反应器(14)。 这些部分以比反应器(14)中低的压力保持在其中。 引入到直接热交换器部分(15)但是在热处理之前的污泥通过与由从排出通道引入蒸发器部分(16)的热处理污泥产生的蒸汽直接接触而被预热 )。
    • 95. 发明公开
    • 유기 폐기물을 이용한 가스제조장치
    • 使用有机废物的气体制造系统
    • KR1020100043706A
    • 2010-04-29
    • KR1020080102862
    • 2008-10-21
    • 주성호
    • 주성호
    • C02F11/04
    • Y02E50/343Y02W10/23C02F11/04C02F2201/002C02F2201/005Y02W10/20
    • PURPOSE: A gas producing apparatus using organic waste is provided to decompose the crushed organic waste into gas including methane gas, carbon dioxide and bad smell gas using an anaerobic fermentation, and to supply the methane gas to a combustion unit. CONSTITUTION: A gas producing apparatus using organic waste comprises the following: a crushing unit(130) crushing the organic waste discharged from a pre-processing unit(100); a storage storing the crushed organic waste; an oxidation tank(220) oxidizing the organic waste transferred by an oxidation tank pump(210); a digestion tank(310) dividing the organic waste into gas and manure fluid by an anaerobic fermentation; and a fluid stabilizing tank(410) separating the fluid into the gas and liquid fertilizer. A inorganic material discharging unit(700) is installed on a pit of the bottom of the oxidation tank. A mixing unit(230) is connected to the lower inner wall of the oxidation tank corresponding to the pit.
    • 目的:提供一种使用有机废物的气体生成装置,使用厌氧发酵将破碎的有机废物分解成包括甲烷气体,二氧化碳和不良气味的气体,并将甲烷气体供应到燃烧单元。 构成:使用有机废弃物的气体生成装置包括:破碎装置(130),破碎从预处理装置(100)排出的有机废弃物; 储存有破碎的有机废物的储存器; 氧化罐(220),氧化由氧化罐泵(210)转移的有机废物; 消化罐(310)通过厌氧发酵将有机废物分解成气体和粪便液体; 以及将流体分离成气体和液体肥料的流体稳定罐(410)。 无机材料排出单元(700)安装在氧化罐底部的凹坑上。 混合单元(230)连接到对应于凹坑的氧化罐的下内壁。
    • 96. 发明授权
    • 하수슬러지 전처리 방법
    • 废污泥预处理方法
    • KR100948494B1
    • 2010-03-18
    • KR1020090065616
    • 2009-07-17
    • 에스워터(주)남궁규철
    • 남궁규철
    • C02F1/34C02F1/78C02F11/00C02F11/04
    • C02F1/34C02F1/78C02F11/00C02F11/04C02F2303/06
    • 본 발명은 하수슬러지 전처리 방법에 관한 것으로서, 오존발생장치로부터 발생되는 오존을 수력학적 캐비테이션을 일으키는 장치의 전단(前段) 또는 후단(後段)에서 슬러지에 주입함으로써, 수력학적 캐비테이션과 오존의 시너지 효과를 불러일으켜 슬러지 구조를 파괴하고 세포막을 파괴하며, 그 결과 슬러지를 가용화함으로써 슬러지의 감량화, 슬러지 탈수능의 향상, 혐기성 소화 효율 향상 등을 하나의 공정으로 종합적으로 이루어내기 위한 하수슬러지 전처리 방법 및 상기 방법을 이용한 하수슬러지 전처리 장치에 관한 것이다. 상기 하수슬러지 전처리 장치는 오존발생장치와 적절한 간격으로 최적화되어 배치되어 있는 오존 주입부를 갖는 배관, 그리고 고압, 고속으로 슬러지를 이송할 수 있는 펌프(모터 포함)에 의해 작은 단면적을 갖는 원형, 타원형, 또는 다각형 모양의 오리피스(orifice)를 통과시켜 수력학적 캐비테이션 현상을 일으키는 장치로 이루어진다.
      하수슬러지 전처리, 캐비테이션, 오존
    • 100. 发明公开
    • 유기성 슬러지 가압치환 감압 건조 처리 시스템, 방법
    • 通过加压取代处理有机污泥的系统,方法和预处理模块,减少加压干燥
    • KR1020090128858A
    • 2009-12-16
    • KR1020080054822
    • 2008-06-11
    • 건민산업 주식회사
    • 박경만
    • C02F11/12C02F11/04C02F9/00
    • C02F11/12C02F9/00C02F11/04Y02W10/20
    • PURPOSE: A system for pressurized-substitution and reduced-pressurized drying of organic sludge and a method therefor are provided to reduce cost for fuelization of the organic sludge and energy consumption, so as to remove moisture of the organic sludge effectively. CONSTITUTION: A system for pressurized-substitution and reduced-pressurized drying of organic sludge comprises the followings: a pre-treating unit(110) mixing the organic sludge and media oil; a pressurized-substitution unit(120) performing reaction between moisture in the organic sludge and the media oil; a solid flowing water separation unit(130) separating solid powder of the sludge from the media oil and the moisture; a first flowing water separation unit(140) separating the media oil and the moisture; a reduced-pressurized drying unit(150) removing remaining moisture; and a solid-liquid separation unit(170) separating the solid powder and the media oil. The system for pressurized-substitution and reduced-pressurized drying of the organic sludge treats moisture removed from the organic sludge by further including a condenser(180), a second flowing water separating unit(142), and a water processing unit(190).
    • 目的:提供有机污泥的加压取代和减压干燥系统及其方法,以降低有机污泥的加油成本和能源消耗,有效去除有机污泥的水分。 构成:有机污泥的加压取代和减压干燥系统包括以下步骤:将有机污泥和介质油混合的预处理单元(110); 加压取代单元(120),其进行有机污泥中的水分与介质油的反应; 将固体粉末与介质油和水分分离的固体流动水分离单元(130); 分离介质油和水分的第一流动水分离单元(140); 减压干燥单元(150)去除剩余的水分; 和分离固体粉末和介质油的固液分离单元(170)。 进一步包括冷凝器(180),第二流水分离单元(142)和水处理单元(190),用于有机污泥的加压取代和减压加压干燥的系统处理从有机污泥中除去的水分。