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    • 1. 发明公开
    • 고온 2차 반응기를 이용한 타르 무배출 바이오매스 가스화 방법
    • 将高温二次反应器生物质吸收至无气体合成气的方法
    • KR1020120074088A
    • 2012-07-05
    • KR1020100136047
    • 2010-12-27
    • 재단법인 포항산업과학연구원
    • 고대권
    • C10J3/00C10K1/00
    • C10J3/02C10J3/20C10J3/84C10K1/00
    • PURPOSE: A tar-free biomass gasifying method using a high-temperature secondary reactor is provided to supply synthetic gas generated from a fluidized-bed gasifier to the high-temperature secondary reactor for removing tar. CONSTITUTION: A tar-free biomass gasifying method using a high-temperature secondary reactor comprises the following steps: inserting solid fuel into a fluidized-bed gasifier(110) with air, oxygen or steam to obtain synthetic gas(130) containing tar and discharge ash(140) containing unburned carbon; supplying the synthetic gas to the high-temperature secondary reactor(120), and inserting particle or liquid waste(150) with air or oxygen into the high-temperature secondary reactor for combusting at the temperature greater than 1,000 deg C; extracting tar-free synthetic gas(160) from the high-temperature secondary reactor; and inserting the ash containing the unburned carbon into the high-temperature secondary reactor, and maintaining the temperature of the high-temperature secondary reactor at 1,200-1,300 deg C before increasing the temperature at 1,400-1,500 deg C for re-combusting the unburned carbon.
    • 目的:提供一种使用高温二次反应器的无焦炭生物质气化方法,将从流化床气化器产生的合成气体提供给用于除去焦油的高温二次反应器。 构成:使用高温二次反应器的无焦炭生物质气化方法包括以下步骤:将固体燃料通过空气,氧气或蒸汽将流化床气化器(110)插入,以获得含有焦油和放电的合成气(130) 含有未燃碳的灰分(140) 将合成气体供应到高温二次反应器(120),并将空气或氧气的颗粒物或废液(150)插入到高温二次反应器中,以在大于1000℃的温度下燃烧; 从高温二次反应器中提取无焦油合成气(160); 将含有未燃烧碳的灰
      料插入高温二次反应器中,并在升高1400-1500℃的温度之前将高温二级反应器的温度保持在1,200-1300℃以再燃未燃碳 。
    • 2. 发明公开
    • Utilization method of coke oven gas or coal gasifier gas
    • 焦炉煤气或煤气化气的利用方法
    • KR20120035348A
    • 2012-04-16
    • KR20100096813
    • 2010-10-05
    • POSCO
    • CHUNG JIN KYUNGKIM SEONG YEON
    • C10B27/00C10J3/00C10K1/00C21B13/00
    • C10K1/00
    • PURPOSE: A utilization method of coke oven gas or coal gasifier gas is provided to diminish use of coal cost and the generation of the CO 2 by using heat of the reducing gas of high temperature. CONSTITUTION: A utilization method of coke oven gas or coal gasifier gas is as follows. The reducing gas of high temperature exhausted from the coke oven or the coal gas burner is partly oxidized to steam and oxygen. The heat of the oxidized reducing gas is exchanged through a plurality of heat exchangers. The reducing gas exhausted in the heat exchanger' is blown into a flowpath to fine ore.
    • 目的:提供焦炉煤气或煤气化炉气的利用方法,以减少使用煤炭成本,并通过使用高温还原气体的热量生成二氧化碳。 构成:焦炉煤气或煤气化炉气的利用方法如下。 从焦炉或煤气燃烧器排出的高温还原气体被部分氧化成蒸气和氧气。 氧化还原气体的热量通过多个热交换器进行交换。 在热交换器中排出的还原气体被吹入细矿石的流路。
    • 3. 发明公开
    • 오프가스 스트림의 처리 방법 및 장치
    • 处理关闭气流及其装置的方法
    • KR1020120008523A
    • 2012-01-30
    • KR1020117026476
    • 2010-04-06
    • 쉘 인터내셔날 리써취 마트샤피지 비.브이.
    • 슈뢰더산드라
    • B01D53/14B01D53/50B01D53/52C10L3/10
    • B01D53/1456B01D53/50B01D53/526B01D53/75B01D2257/308B01D2257/406C10J2300/0909C10J2300/093C10J2300/1681C10K1/00C10K1/003C10K1/12Y02P20/152
    • 본 발명은, 황산염 스트림 (910) 을 제공하기 위해 NH
      3 및 H
      2 S 를 포함하는 오프가스 스트림 (80) 을 처리하는 방법으로서, (ⅰ) NH
      3 , H
      2 S, CO
      2 , 및 선택적으로 HCN, COS 와 CS
      2 중 1 이상을 포함하는 제 1 오프가스 스트림 (80) 을 제공하는 단계; (ⅱ) 상기 제 1 오프가스 스트림 (80) 을 소각로 (300) 로 전달하여, NH
      3 , H
      2 S, 및 선택적으로 HCN, COS 와 CS
      2 중 1 이상을 산화시켜서, N
      2 , H
      2 O, SO
      2 및 CO
      2 를 포함하는 제 2 오프가스 스트림 (310) 을 제공하는 단계; (ⅲ) 부식성 스크러버 (350) 에서 제 2 오프가스 스트림 (310) 을 제 1 수성 알칼리 스트림 (380, 876a) 으로 스크러빙하여, 제 2 오프가스 스트림으로부터 SO
      2 및 CO
      2 의 일부를 분리하여서, 탄산염 및 아황산염과 중아황산염의 일방 또는 쌍방을 포함하는 소비된 부식성 스트림 (360), 및 N
      2 및 CO
      2 를 포함하는 부식성 스크러버 오프가스 스트림 (370) 을 제공하는 단계; 및 (ⅳ) 소비된 부식성 스트림 (360) 을, 산소의 존재 하에서 황 산화 박테리아를 포함하는 폭기장치 (900) 로 전달하여, 아황산염 및 중아황산염을 황산염으로 생물학적으로 산화시켜서, 황산염 스트림 (910) 을 제공하는 단계를 포함하는 방법을 제공한다.
    • 本发明提供了一种处理包含NH 3和H 2 S的废气流(80)以提供硫酸盐流(910)的方法,所述方法包括以下步骤:(i)提供第一废气流(80),其包括 NH 3,H 2 S,CO 2和任选的一种或多种HCN,COS和CS2; (ii)将第一废气流(80)通过焚烧炉(300)以氧化NH 3,H 2 S以及任选的一种或多种HCN,COS和CS2以提供包含N 2的第二废气流(310) H2O,SO2和CO2; (iii)用苛性碱洗涤器(350)中的第一含水碱性物流(380,876a)洗涤所述第二尾气物流(310)以从所述第二废气流分离SO 2和一部分CO 2以提供 包含碳酸盐和一种或两种亚硫酸盐和亚硫酸氢盐的废碱流(360)和包含N 2和CO 2的苛性洗涤器废气流(370); 和(iv)在氧气存在下将废碱流(360)传递到包含硫氧化细菌的曝气器(900)以生物氧化亚硫酸盐和亚硫酸氢盐至硫酸盐以提供硫酸盐流(910)。
    • 4. 发明公开
    • 코크스오븐가스 정제설비용 맨홀장치
    • 用于净化烤箱装置的锅炉装置
    • KR1020120132785A
    • 2012-12-10
    • KR1020110051128
    • 2011-05-30
    • 현대제철 주식회사
    • 김진한정상중박현수유진욱
    • C10B45/00B65D90/10
    • C10B45/00B65D90/10C10K1/00
    • PURPOSE: A manhole apparatus for a cokes oven gas purifying device is provided to improve work efficiency in coupling and decoupling of a manhole cover to a connecting unit by easily regulating the height of a heavy manhole cover with an operating member. CONSTITUTION: A manhole apparatus for a cokes oven gas purifying device comprises a connecting unit(20), a manhole cover(30), a rotating unit(40), and a height regulating unit(50). The connecting unit is connected to the inside of the cokes oven gas purifying device. The manhole cover is coupled to the connecting unit. The rotating unit is connected to a supporting unit and rotates the manhole cover. The height regulating unit connects the rotating unit to the manhole cover and regulates the height of the manhole cover.
    • 目的:提供一种用于焦炉炉气体净化装置的人孔装置,通过容易地利用操作构件调节重型人孔盖的高度来提高人孔盖与连接单元的联接和分离的工作效率。 构成:用于焦炉炉气体净化装置的人孔装置包括连接单元(20),人孔盖(30),旋转单元(40)和高度调节单元(50)。 连接单元连接到焦炉煤气净化装置的内部。 人孔盖连接到连接单元。 旋转单元连接到支撑单元并旋转井盖。 高度调节单元将旋转单元连接到人孔盖,并调节井盖的高度。
    • 9. 发明公开
    • 가스선별장치 및 방법
    • 用于分配气体的装置和方法
    • KR1020140041136A
    • 2014-04-04
    • KR1020120108148
    • 2012-09-27
    • 현대제철 주식회사
    • 김구용박병철
    • C21C5/38F27D17/00C10K1/00
    • Y02P10/212C21C5/38C10K1/00F27D17/00
    • A gas sorting apparatus and a gas sorting method are disclosed. The gas sorting apparatus comprises: a first pipe into which a converter gas flows; a first measuring instrument measuring a carbon monoxide content in the converter gas flowing into the first pipe; a second pipe connected to the first pipe, and delivering the converter gas to a mixing part when the carbon monoxide content measured by the first measuring instrument is smaller than a reference value; a second measuring instrument installed at the second pipe, and measuring an oxygen content in the converter gas flowing into the mixing part; a third pipe into which a blast furnace gas flows; a fourth pipe branching off from the third pipe and connected to the mixing part; a fifth pipe connected to the third pipe and transferring the blast furnace gas; a flow rate control valve installed at the fourth pipe, and controlling the flow rate of the blast furnace gas delivered to the mixing part; a sixth pipe delivering a mixed gas, which is discharged from the mixing part, to the fifth pipe; a calorie measuring instrument installed at the sixth pipe and measuring calories in the mixed gas; and a control part controlling the operation of the flow rate control valve using the oxygen content measured by the second measuring instrument and the calories measured by the calorie measuring instrument.
    • 公开了一种气体分选装置和气体分选方法。 气体分选装置包括:转炉气体流过的第一管道; 测量流入第一管道的转化器气体中的一氧化碳含量的第一测量仪器; 连接到第一管道的第二管道,并且当由第一测量仪器测量的一氧化碳含量小于参考值时,将转化器气体输送到混合部件; 第二测量仪器,安装在第二管道处,并测量流入混合部件的转炉气体中的氧含量; 高炉煤气流过的第三个管道; 从第三管分支并连接到混合部分的第四管; 连接到第三管并传送高炉煤气的第五管; 安装在第四管道处的流量控制阀,并控制输送到混合部件的高炉煤气的流量; 将从混合部排出的混合气体输送到第五管道的第六管道; 安装在第六管道上的卡路里测量仪器,并测量混合气体中的卡路里; 以及控制部,其使用由所述第二测量仪测量的氧含量和由所述卡路里测量仪测量的卡路里来控制所述流量控制阀的操作。
    • 10. 发明公开
    • 코크스 오븐 가스 처리 장치 및 방법
    • 用于处理焦炉煤气的装置和方法
    • KR1020120114573A
    • 2012-10-17
    • KR1020110032172
    • 2011-04-07
    • 재단법인 포항산업과학연구원
    • 박주형
    • C10B57/00C10K1/02C10K1/04C10B45/00
    • C10B57/00C10K1/00C10K1/02C10K1/04C10K3/00C10L3/101
    • PURPOSE: A coke oven gas treatment apparatus and a method are provided to reduce carbon dioxide as reducing gas is blown into a blast furnace or a flow path in an iron making process. CONSTITUTION: A coke oven gas treatment apparatus comprises a first coke oven gas treating unit(100) and a second coke oven gas treating unit(200). The first coke oven gas treating unit is connected to the lower part of a riser tube in a COG(Coke Oven Gas) carbonization chamber(10). The second coke oven gas treating unit is connected to the riser tube. The first and second coke oven gas treating units are successively operated, and treat the COG. [Reference numerals] (AA) Coke oven gas(CH4-rich gas); (BB) Coke oven gas(H2/CO-rich gas)
    • 目的:提供一种焦炉气体处理装置和一种方法,用于在制铁过程中将高压炉或流路中的还原气体吹入时减少二氧化碳。 构成:焦炉气体处理装置包括第一焦炉气体处理单元(100)和第二焦炉气体处理单元(200)。 第一焦炉气体处理单元连接到COG(焦炉炉)碳化室(10)中的提升管的下部。 第二焦炉气体处理单元连接到提升管。 第一和第二焦炉煤气处理装置相继运行,并处理COG。 (AA)焦炉煤气(富CH4气体); (BB)焦炉煤气(H2 / CO富气)