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公开(公告)号：KR102205773B1
公开(公告)日：2021-01-21
申请号：KR1020180155748
申请日：2018-12-06
Applicant: 한국에너지기술연구원
Abstract: 본발명은내통및 외통을포함하는이중층구조의본체부, 상기본체부상부에구비되는덮개, 상기본체부의외부와내부를관통하는가스배출관, 상기가스배출관과상기본체부를연결하는가스순환관, 상기가스배출관외주변에배열되며, 일측단부는상기덮개외부로돌출되고, 타측단부는내통에위치하는복수개의피건조물공급부재, 및본체부와연결된 '+' 리드선과상기가스순환관과연결된 '-' 리드선을포함하는전원공급부(80)를포함하고, 상기내통의외면에는가스유입구가형성되고, 상기외통의외면에는가스배출구가형성되는정전분무사이클론건조기에관한것이다.
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Patent Agency Ranking
公开(公告)号：KR102198334B1
公开(公告)日：2021-01-05
申请号：KR1020180155734
申请日：2018-12-06
Applicant: 한국에너지기술연구원
Abstract: 본발명은수직형태로공급되는물에의한정전분무노즐에서발생하는쇼트또는정전분무가발생하지않는등의문제를해결하기위한물의수두차를이용한정전분무다중노즐및 이를포함하는습식집진장치에관한것으로이러한미세액적과배기가스를접촉시키기때문에, 입경이작은입자의제거효율을향상시킬수 있다는장점및 원통부중심에복수의관로를형성하여수두차에의한물의공급을통해정전분무를효과적으로발생시킬수 있는효과가있다.
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公开(公告)号：KR101549832B1
公开(公告)日：2015-09-03
申请号：KR1020130126565
申请日：2013-10-23
Applicant: 한국에너지기술연구원
IPC: B01D33/06 , B01D33/073 , B01D36/00 , B01D25/00
Abstract: 본발명은함수율이 99wt% 이상인고함수율상태의현탁액을 90~95wt%인슬러리형태의현탁액으로농축시킬수 있도록하여별도의탈수장치를이용하여목표함수율까지탈수속도증가와탈수비용을절감할수 있도록한 회전식진공농축장치에관한것으로, 이를위해고함수율의현탁액이공급되는원통챔버의내부에다공드럼을마련하고, 상기다공드럼의내부에진공을걸어현탁액에포함된수분을흡수함에따라최종적으로배출되는현탁액을농축할수 있도록구성되는것을특징으로한다.
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公开(公告)号：KR101327268B1
公开(公告)日：2013-11-08
申请号：KR1020110140686
申请日：2011-12-23
Applicant: 한국에너지기술연구원
Abstract: 본 발명은 각종 실험실, 반도체 산업, 시약제조 및 병원 검사실 등 다양한 분야에서 사용되는 수증기, 증류수 제조장치 및 이들의 제조방법에 관한 것으로서, 자세하게는 증류수를 만드는데 필수적인 수증기의 제조 열원으로 전기 대신에 도시가스 또는 LPG와 같은 연료가스를 촉매버너로 연소하여 발생한 연소열을 사용하는 것을 특징으로 하는 수증기, 증류수 제조장치 및 이들의 제조방법에 대한 것이다.
본 발명에 따른 수증기, 증류수 제조장치 및 제조방법은 촉매버너에서 발생한 원적외선 복사에너지 형태의 열을 수증기 제조에 활용함으로써 매우 높은 에너지 효율을 구현할 수 있다.-
公开(公告)号：KR101288041B1
公开(公告)日：2013-07-19
申请号：KR1020120035661
申请日：2012-04-05
Applicant: 한국에너지기술연구원
Abstract: PURPOSE: A multi-stage integrated dryer using a swirling current is provided to reduce the size by integrating through inserting a second cyclone a hot air drying cylinder into a current drying cylinder. CONSTITUTION: A multi-stage integrated dryer (100) using a swirling current comprises a current drying cylinder (10), a first cyclone (20), a how air drying unit (30), a heat exchanger (40), and a hot air supply pipe (50). The current drying cylinder firstly dries a dried object (70) at room temperature through the swirling current at a high speed in increased room temperature and discharges to the outside. The how air drying unit includes a second cyclone (31) with a second exhaust pipe (311) inducing the hot air to the heat exchanger. The second cyclone is arranged in the center of the current drying cylinder.
Abstract translation: 目的：提供使用旋流电流的多级一体式干燥器，通过将热风干燥筒的第二旋风分离器插入到当前的干燥筒中来整合来减小尺寸。 构成：使用旋转电流的多级一体式干燥器（100）包括当前的干燥筒（10），第一旋风分离器（20），空气干燥单元（30），热交换器（40）和热 供气管（50）。 目前的干燥筒首先在室温下通过旋转电流在室温下以高速在室温下干燥干燥物体（70）并将其排出到外部。 空气干燥单元如何包括具有第二排气管（311）的第二旋风分离器（311），该排气管将热空气引导到热交换器。 第二旋风分配器设置在当前干燥筒的中心。
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公开(公告)号：KR1020130013385A
公开(公告)日：2013-02-06
申请号：KR1020110075008
申请日：2011-07-28
Applicant: 한국에너지기술연구원
CPC classification number: C10J3/84 , B01D53/06 , B01J8/24 , C10J3/34 , C10J2300/1628
Abstract: PURPOSE: A tar refinement and recovery apparatus is provided to use a solid particle using fluidized bed gasifier, thereby minimizing the operation cost and the installation cost of subsequent facilities. CONSTITUTION: A tar refinement and recovery apparatus comprises the following steps: A fluidized bed gasifier(10) thermal cracks solid particles and steam by a high temperature-fluid sand, and produces synthetic gas whose main ingredients are H2 and CO. The first gas separator(20) discharges dusts and fluid sand included in the synthetic gas, and separates the synthetic gas. A tar remover(30) adsorbs the tar included in the synthetic gas on the surface of the solid particle, and discharges the solid particle with the synthetic gas. The second gas separator(40) discharges the solid particle that the tar is adsorbed on, restores in the fluidized bed gasifier, and separate the synthetic gas. A refinement filter(50) refines the supplied synthetic gas to a usable synthetic fuel. A chamber(11) has a recovery inlet(111) formed in the side for the solid particle restored from the second gas separator to be reused as a heating material for the fluid sand, and a fire hole(112) discharging the combustion gas of the heating material. The first duct(12) has the first inlet port(121) separating the heated fluid sand from the chamber inside and injecting the solid particle, and a steam supply globe(122) supplying steam. A fluid sand duct(13) is formed in the side of the first duct in a line, and the fluid sand rising through the first duct drops and re-flows in the fluid sand duct. A perforated hole(123) is formed in the lower part of the first duct for biomass to be thermal cracked directly by the fluid sand. A cyclone(21) is connected to a discharger(211) for the solid particle to be discharged to the lower part, and for the synthetic gas to be transmitted to the upper end. [Reference numerals] (AA) Cooling water; (BB) Fluid sand; (CC) Tar; (DD) Bio mass; (EE) Bio mass absorbed with tar; (FF) Syngas; (GG) Steam; (HH) Combustion gas
Abstract translation: 目的：提供使用流化床气化器的固体颗粒的焦油精炼和回收设备，从而最大限度地降低后续设施的运行成本和安装成本。 构成：焦油精炼和回收装置包括以下步骤：流化床气化炉（10）通过高温流体砂热固裂颗粒和蒸汽，产生主要成分为H2和CO的合成气，第一气分离器 （20）排出包含在合成气体中的灰尘和流体砂，并分离合成气体。 焦油去除剂（30）吸附固体颗粒表面上合成气体中包含的焦油，并用合成气体排出固体颗粒。 第二气体分离器（40）排出焦油吸附的固体颗粒，在流化床气化器中还原，分离合成气体。 细化过滤器（50）将供应的合成气体精炼成可用的合成燃料。 室（11）具有形成在从第二气体分离器恢复的固体颗粒侧的回收入口（111），作为用于流体砂的加热材料被再利用，以及将燃烧气体排出的火孔（112） 加热材料。 第一管道（12）具有将加热的流体砂与室内分离并注入固体颗粒的第一入口（121）和供应蒸汽的蒸汽供应球体（122）。 流体砂管（13）在第一管道的一侧形成一行，并且通过第一管道上升的流体砂落在流体砂管道中再流动。 在第一管道的下部形成有孔（123），用于生物质直接被流体砂热破裂。 旋流器（21）连接到排出器（211），用于固体颗粒排放到下部，并且合成气体被传送到上端。 （标号）（AA）冷却水; （BB）流砂; （CC）焦油; （DD）生物质量; （EE）用焦油吸收的生物质量; （FF）合成气; （GG）蒸汽; （HH）燃烧气体
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