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公开(公告)号：KR101242691B1
公开(公告)日：2013-03-12
申请号：KR1020100135919
申请日：2010-12-27
Applicant: 재단법인 포항산업과학연구원
IPC: C21B3/06
CPC classification number: Y02W30/543
Abstract: 용융 슬래그 미립화 장치가 개시된다. 개시된 용융 슬래그 미립화 장치는 고온의 용융 슬래그로부터 열 에너지를 회수하기 위해 용융 슬래그를 미세한 입자들로 미립화시키는 것으로서, ⅰ)고온의 용융 슬래그가 투입될 수 있는 챔버와, ⅱ)챔버의 내부에 회전 가능하게 구성되며 원심력에 의해 가장자리에서 용융 슬래그의 액적을 형성하는 회전 디스크와, ⅲ)챔버에 장착되며 회전 디스크 상의 용융 슬래그를 가열하는 적어도 하나의 가열 버너와, ⅳ)챔버에 구성되며 용융 슬래그의 온도를 측정하고 그 측정값을 제어기로 출력하는 온도 측정 센서를 포함하여 이루어진다.
Abstract translation: 公开了一种熔融炉渣雾化装置。 所公开的熔融炉渣雾化设备将熔融的炉渣雾化成细颗粒以回收来自热熔渣的热能，该设备包括：i）可将热熔渣导入其中的腔室;以及ii） 并且至少一个加热燃烧器安装在腔室中并加热旋转盘上的熔渣; iv）温度控制器，配置在腔室中并构造成控制熔渣的温度 并将测量值输出到控制器。
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公开(公告)号：KR1020120099969A
公开(公告)日：2012-09-12
申请号：KR1020110018528
申请日：2011-03-02
Applicant: 재단법인 포항산업과학연구원
Inventor： 박흥수
IPC: F27D17/00
CPC classification number: Y02P10/143 , Y02P10/283 , Y02P80/152 , F27D17/004 , C10J1/20 , C10J2300/1853 , F27D99/0033 , F27D2017/006
Abstract: PURPOSE: A heat recovery type heating furnace and a heat recovery method using the same are provided to recover the heat of exhaust gas to be used for preheating combustion gas and for producing steam that reacts with methane gas supplied to a burner. CONSTITUTION: A heat recovery type heating furnace comprises a steam generating unit(20) and a gas reforming unit(30). The steam generating unit is located inside a flue(10) and generates steam using high-temperature exhaust gas discharged through the flue. The gas reforming unit is located inside the flue and connected to the steam generating unit, and the gas forming unit mixes the steam and methane gas to react with each other and produce carbon monoxide and hydrogen.
Abstract translation: 目的：提供一种热回收式加热炉及使用其的热回收方法，以回收用于预热燃烧气体的废气的热量，并产生与供给燃烧器的甲烷气体反应的蒸汽。 构成：热回收型加热炉包括蒸汽发生单元（20）和气体重整单元（30）。 蒸汽发生单元位于烟道（10）的内部，并使用通过烟道排出的高温废气产生蒸汽。 气体重整单元位于烟道内并连接到蒸汽发生单元，气体形成单元将蒸汽和甲烷气体相互混合，产生一氧化碳和氢气。
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公开(公告)号：KR101173499B1
公开(公告)日：2012-08-14
申请号：KR1020100136693
申请日：2010-12-28
Applicant: 주식회사 포스코 , 재단법인 포항산업과학연구원
IPC: C21B3/06
CPC classification number: Y02W30/543
Abstract: 본 발명은 상면에 낙하하는 용융 슬래그를 입자 슬래그로 변환시키고, 상기 입자 슬래그를 비산시키는 회전 원판부; 상기 회전 원판부의 측면에 이격된 상태로 위치되고, 상기 회전 원판부로부터 비산된 입자 슬래그와 충돌하여 상기 충돌된 입자 슬래그를 하측으로 이동시키는 회전 드럼부; 및 상기 회전 드럼부를 향하여 위치되어 상기 회전 드럼부에 냉각수와 압축공기의 혼합물을 분사하는 분사 노즐부를 포함하되, 상기 혼합물이 분사된 회전 드럼부는 냉각되어, 상기 충돌된 입자 슬래그를 냉각시키는 것을 특징으로 하는 용융 슬래그의 조립화 장치를 개시한다. 상기와 같은 용융 슬래그의 조립화 장치는 조립화된 입자 슬래그의 재융착 및 장치의 벽면에 입자 슬래그의 부착을 방지한다.
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公开(公告)号：KR1020120073982A
公开(公告)日：2012-07-05
申请号：KR1020100135920
申请日：2010-12-27
Applicant: 재단법인 포항산업과학연구원
IPC: C21B3/06
CPC classification number: Y02W30/543 , C21B3/06 , F27D15/00 , F27D21/0014
Abstract: PURPOSE: An apparatus for atomizing molten slag is provided to prevent the generation of agglomerated slag on a surface of a rotary disc because the amount of heat delivered to the rotary disc is minimized. CONSTITUTION: An apparatus(100) for atomizing molten slag comprises a chamber(10) and a rotary disc(30). High temperature molten slag is putted into the chamber. The rotary disc is rotatably installed inside the chamber. The rotary disc forms molten slag droplets by centrifugal force at the edge. The rotary disc comprises first and second disc members(41,51). The first disc member is made of steel materials. The second disc member is made of ceramic materials, and connected to the upper surface of the first disc member.
Abstract translation: 目的：提供一种用于雾化熔渣的装置，以防止在旋转盘的表面上产生凝聚的炉渣，因为传送到旋转盘的热量最小化。 构成：用于雾化熔渣的设备（100）包括室（10）和旋转盘（30）。 将高温熔渣放入室内。 旋转盘可旋转地安装在腔室内。 旋转盘通过离心力在边缘形成熔渣液滴。 旋转盘包括第一和第二盘构件（41,51）。 第一盘片由钢材制成。 第二盘片由陶瓷材料制成，并连接到第一盘片的上表面。
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公开(公告)号：KR101082127B1
公开(公告)日：2011-11-10
申请号：KR1020090132722
申请日：2009-12-29
Applicant: 재단법인 포항산업과학연구원
IPC: C10B45/00
Abstract: 본발명은코크스오븐에서발생하는폐열을이용하여고온탄소를이산화탄소및/또는물과반응시켜코크스오븐가스(coke oven gas, COG)를증량시키는방법에관한것으로서, 보다구체적으로는코크스오븐의탄화실에서코크스오븐가스(COG) 스트림에이산화탄소, 물또는이들의혼합물인가스화제를공급하는단계; 및상기가스화제를탄화실내의탄소와반응시켜탄소를가스화하는단계를포함하는코크스오븐가스의증량방법및 이에적합한코크스오븐장치를제공한다.
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Patent Agency Ranking
公开(公告)号：KR101077164B1
公开(公告)日：2011-10-27
申请号：KR1020090131817
申请日：2009-12-28
Applicant: 재단법인 포항산업과학연구원
CPC classification number: Y02W30/542
Abstract: 슬래그입자의이동방향과유동방향이동일한상온의공기를 2단으로분사할수 있도록단계적으로구현함으로써, 입자들을급랭시켜슬래그입자간의재융착현상을방지하여동일공기유량에대한열전달효율을향상시키는효과가있다.
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公开(公告)号：KR101071500B1
公开(公告)日：2011-10-10
申请号：KR1020030066971
申请日：2003-09-26
Applicant: 재단법인 포항산업과학연구원
Inventor： 박흥수
IPC: F23D14/84
Abstract: 개시된발명은연소로내의질소산화물발생저감장치및 방법에관한것으로, 연소가열공정에대하여설비의개조또는교체소요를줄이면서저 비용으로질소산화물생성을저감시키기위한것이다. 이를위하여본 발명은난류확산버너가설치된연소로의질소산화물발생저감장치에있어서, 상기연소로의측벽에개구부를형성하고, 상기연소로의측벽개구부에음향부가장치를설치하여상기연소로의내부로유체밀도의변동을유도할수 있는음파를부가하도록구성하는연소로의질소산화물발생저감장치및 방법을제공하며, 기존에설비되어있는버너장치를교체하지않고도연소로에서발생되는질소산화물을저감시킬수 있고, 또한질소산화물저감을위하여저 질소산화물생성형버너로교체한경우에있어서도추가적인질소산화물생성억제가가능하게되며, 따라서질소산화물생성억제를위한경비절감및 환경보전에기여할수 있는등의이점을얻을수 있게된다.
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公开(公告)号：KR1020110076106A
公开(公告)日：2011-07-06
申请号：KR1020090132722
申请日：2009-12-29
Applicant: 재단법인 포항산업과학연구원
IPC: C10B45/00
Abstract: PURPOSE: A method for amplifying coke-oven gas using carbon dioxide is provided to minimize the use of high-temperature heat energy by using the waste heat of coke-oven gas and high-temperature carbon. CONSTITUTION: A method for amplifying coke-oven gas using carbon dioxide is as follows. A gasifying agent, which is a mixture of carbon dioxide and water, is supplied to the upper part of a Coke-Oven Gas stream at a carbonizing chamber(4). The supplied COG stream is stayed at the carbonizing chamber for 5 to 60 seconds. Carbon inside the carbonizing chamber is gasified by reacting with the gasifying agent.
Abstract translation: 目的：提供使用二氧化碳放大焦炉煤气的方法，通过使用焦炉煤气和高温碳的废热来最大限度地减少高温热能的使用。 构成：使用二氧化碳放大焦炉气体的方法如下。 作为二氧化碳和水的混合物的气化剂在碳化室（4）供给到焦炉煤气流的上部。 所供应的COG流在碳化室中停留5至60秒。 碳化室内的碳与气化剂反应气化。
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公开(公告)号：KR1020110075375A
公开(公告)日：2011-07-06
申请号：KR1020090131816
申请日：2009-12-28
Applicant: 재단법인 포항산업과학연구원
CPC classification number: Y02W30/542
Abstract: PURPOSE: An apparatus and a method for recovering excess heat from molten slag are provided to effectively recover the excess heat through a miniaturized facility using a physical heat exchange and chemical reaction. CONSTITUTION: A heating duct(1) delivers a mixed gas including carbon dioxide through one side of a chamber(4). A swirler(7) is formed on an end of the heating duct and allows the mixed gas to form vortex and react with molten slag(5). The used gas is discharged together with granulated slag to an exit(6) of the chamber. A heater(3) is installed in the front end of the heating duct and preheats the mixed gas.
Abstract translation: 目的：提供一种用于从熔渣回收多余热量的装置和方法，以通过物理热交换和化学反应有效地通过小型化设备回收多余的热量。 构成：加热管道（1）通过室（4）的一侧输送包括二氧化碳的混合气体。 旋流器（7）形成在加热管道的一端，允许混合气体形成涡流并与熔渣（5）反应。 废气与造粒渣一起排出到室的出口（6）。 加热器（3）安装在加热管道的前端并预热混合气体。
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公开(公告)号：KR1020110066681A
公开(公告)日：2011-06-17
申请号：KR1020090123428
申请日：2009-12-11
Applicant: 재단법인 포항산업과학연구원
IPC: C01B32/50 , C07C273/04
CPC classification number: Y02A50/2342 , C01B32/50 , B01D8/00 , B01D53/02 , B01D53/62 , B01D2252/2023 , B01D2253/102 , B01D2253/104 , B01D2256/22 , C07C273/04
Abstract: PURPOSE: A urea manufacture method utilizing iron manufacturing process exhaust gas is provided to manufacture the carbon dioxide for the urea manufacture with remarkably low cost by separating, collecting, and refining the carbon dioxide from iron manufacturing process exhaust gas. CONSTITUTION: The urea manufacture method utilizing iron manufacturing process includes the steps of: collecting more than 95% of the carbon dioxide by collecting and separating the carbon dioxide from the iron manufacturing process exhaust gas with chemical absorption or adsorption(i); obtaining carbon dioxide more than 99.5% of the purity by eliminating the moisture, the acid material, and the corrosive material and salt producing material from the collected carbon dioxide(ii); putting the refined carbon dioxide in the urea manufacturing process(iii). The step(ii) includes the steps of: cooling moisture of eliminating moisture using ethylene glycol(a); eliminating acid material, and the corrosive material and salt producing material with adsorption method utilizing activated alumina or activated carbon(b); and eliminating inactivated gas due to the high pressure liquefaction of CO2(c).
Abstract translation: 目的：提供一种利用铁制造工艺废气的尿素制造方法，通过从铁制造工艺废气中分离，收集和精制二氧化碳来制造用于尿素制造的二氧化碳，成本非常低。 构成：利用铁制造工艺的尿素制造方法包括以下步骤：通过从具有化学吸附或吸附的铁制造工艺废气中收集和分离二氧化碳来收集95％以上的二氧化碳（i）; 通过从收集的二氧化碳（ii）中除去水分，酸性物质和腐蚀性材料和盐产生物质，从而获得超过99.5％的纯度的二氧化碳; 将精制二氧化碳置于尿素制造过程中（iii）。 步骤（ii）包括以下步骤：使用乙二醇（a）冷却除去水分的水分; 使用活性氧化铝或活性炭（b）的吸附方法消除酸性物质，腐蚀性物质和盐生产物质; 并且由于CO2的高压液化而消除了灭活气体（c）。
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