• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.107.2-107.2
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• 2010

고온건식탈황기술은 고온고압에서 석탄가스에 함유된 황화합물을 제거하는 기술로 석탄가스화에 의해 생성된 고온의 석탄가스의 열손실을 최소화하여 열효율이 높은 기술이다. 본 연구에서는 석탄으로부터 합성원유를 생산하는 0.3 배럴/일 규모 석탄액화(CTL)공정의 연계운전을 통하여 건식탈황공정의 성능을 평가하였다. 0.3 배럴/일 규모 석탄액화공정은 석탄가스화기, 건식탈황공정, 액화공정으로 구성되어 있으며 30 atm의 고압에서 운전된다. 건식탈황공정은 석탄가스화기와 액화공정 사이에 위치하여 석탄가스화로부터 생성된 석탄가스에 함유된 황화합물을 아연계 건식탈황제에 의해 제거한 후 액화반응기로 공급하여 황화합물에 의한 촉매의 피독을 막아주는 역할을 수행한다. 본 연구에서는 기존에 개발된 두 개의 기포유동층 반응기로 구성된 탈황장치를 30 atm에서 운전이 가능하도록 수정/보완하여 실제 운전압력인 30 atm의 고압에서 연속운전을 수행하였다. 실험 결과 탈황효율은 99% 이상이며 탈황반응기 출구 황화합물의 농도는 1 ppmv 이하로 유지하였다.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2003.05a
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• pp.497-502
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• 2003

청정석탄이용기술개발의(CCT : Clean Coal Technology) 일환으로 차세대 발전방식으로 유력시되고 있는 기술인 석탄가스화발전기술(IGCC), 석탄가스화 연료전지(IGFC)등에서 고온건식탈황은 필수요소기술이다. 고온건식탈황기술의 핵심기술은 탈황제개발고 공정기술개발로 나누어 볼 수 있다. 탈황제개발은 국내고유 탈황제개발 연구가 진행 중에 있고 유동층과 고속유동층에 적합한 탈황제를 kg단위로 성형하여 공정개발에서 반응특성 실험을 하였다.(중략)

• Clean Technology
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• v.8 no.1
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• pp.11-17
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• 2002

Petcokes is the final product obtained from a refinery process. This petcokes includes high percentage of inorganic and sulfur compounds. Currently, the petcokes produced from domestic refinery plants include more than 6% of sulfur. To use petcokes as valuable raw materials, the weight percentage of sulfur must be lower than 2% of sulfur. Solvent extraction, thermal desulfurization, and hydro-desulfurization have been used to remove the sulfur. In this study, we attempted new approach to remove the sulfur introducing microwave energy. Microwave increase the reaction rates by providing the fast heating and disconnecting the bonding structure of the molecules. The experiments of microwave thermal desulfurization and microwave plus hydrogen gas were carried out to remove the sulfur. We obtained 68.3% of sulfur removal rate with the 2 hours of reaction time and 1835 W of microwave powder. In the experiment of microwave with hydrogen gas, we obtained 86.4% of sulfur removal rate with the 1.5 hours of reaction time and 1835 W of microwave power. If we increase reaction time or decrease the particle size of petcokes, we expect more than 90% of sulfur removal.

• Journal of Welding and Joining
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• v.1 no.2
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• pp.7-11
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• 1983

본 공장(진해화학주식회사)에서 암모니아는 나프타를 원료로 한 수소와 공기 중의 질소를 합성하여 제조된다. 암모니아 제조 공정 중 메탄가스(CH$_{4}$)와 수소가스(H$_{2}$) 중에 불순물로 존재하는 유화 수소(H$_{2}$S)를 제거시키는 공정이 탈황공정이다. 탈황공정은 산화 아연(ZnO)과 코발트-몰리브덴(Cobalt-Molybdenum) 촉매층에서 이루어지며 탈황공정이 이루어지는 용기를 탈황조(desulfurizer vessel)라 한다. 본 공장에 설치된 탈황조는 1966년에 설치되어 운용되어 왔다. 본 공장의 안전 조업을 위해 초음파 탐상법, 방사선 투과 탐상법, 표면 침투 탐상법으로써 탈황조의 노후도 측정을 행하였다. 탐상 결과 스테인레스 클래드의 모재부 용접선을 따라 균열이 발견되었다. 균열 부위를 깊이 연마하여 용접 결함부를 제거하고 다시 용접을 함으로써 본 탈황조를 연장하여 사용할 수 있었다.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.1
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• pp.17-22
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• 2010

The aim of this study is to research applicable possibility of DSI (Dry Sorbent Injection) technique in $SO_2$ removal process using lab-scale facility based on 500MW in capacity coal-fired thermal power plant operated by South Korea N. Power Co., Ltd. To increase the $SO_2$ removal efficiency, it is considered the mixing enhancement as different shapes called lobed-plate and stepplate tested ultimately for optimum shape. Also it tested to analysis $SO_2$ removal efficiency by numbers of injection holes. At experimental it showed the $SO_2$ removal efficiency is higher using mixing enhancement than not installed mixing enhancement and case on the step-plate was shown the most $SO_2$ removal efficiency. Also, $SO_2$ removal efficiency was higher recording which will increase the injection holes case on not installed mixing enhancement. But, the $SO_2$ removal efficiency was higher 4 injection holes case on installed mixing enhancement.

• Elastomers and Composites
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• v.35 no.4
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• pp.288-295
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• 2000

It has been tried to decrease the crosslink density of vulcanized EPDM (ethylone-propylene-diene terpolymer) rubber through a chemical devulcanization treatment. Phase transfer catalyst, alkali metal (i.e., sodium), and triphenylphosphine have been used as a chemical agent ul the devulcanization treatment. Also it has been estimated the effect of the devulcanization treatment in the case of utilization of 2-butanol as a devulcanization reaction solvent. In the devulcanization treatment using quaternary ammonium salt as a phase transfer catalyst. the devulcanization effect has been studied with the variation of catalyst molecular weight and the choice of bromide or chloride cation. In the devulcanization treatment using sodium, it has been estimated the devulcanization treatment effect depending upon the variation of reaction variables such as amount of sodium used, reaction temperature, pressure of hydrogen gas, which is used as a reaction environment. The $M_c$ value (number average molecular weight between two crosslink points) has been experimentally estimated by the equilibrium swelling method and it is quantitatively related to the crosslink density. The estimation of devulcanization effect for vulcanized EPDM rubber has been carried out by the comparison of the $M_c$ values between the untreated and the treated specimens.

• Clean Technology
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• v.3 no.1
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• pp.96-105
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• 1997

The objectives of this study were to investigate $SO_2$ removal efficiency of anthracite - bituminous coal blend combustion in a fludized bed coal combustor with Ca/S, anthracite ratio, bed temperature, and waste paper sludge particle size. The experimental results were presented as follow ; the effect of the desulfurization by the particle size of waste paper sludge was a great and $SO_2$ removal efficiency was heigest in paper sludge dia $1016{\mu}m$. And the difference of $SO_2$ removal efficiency according to air velocity was not too large. As Ca/S mole ratio incresed, $SO_2$ removal efficiency incresed rapidly up to Ca/S mole ratio 3 while the desulfurization rates did not increse too largely in the range of more than the level. The bed temperature had a great deal of effect on the desulfurization rate. So the $SO_2$ removal efficiency was a graet using waste paper sludge that the properbility of paper sludge as sorbent was conformed.

• Korean Chemical Engineering Research
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• v.50 no.3
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• pp.492-498
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• 2012

In this study, hydrodynamics such as solid circulation rate and voidage in the desulfurizer and the reaction characteristics of Zn-based solid sorbents were investigated using lab-scale high pressure and high temperature desulfurization process. The continuous HGD (Hot Gas Desulfurization) process consist of a fast fluidized bed type desulfurizer (6.2 m tall pipe of 0.015 m i.d), a bubbling fluidized bed type regenerator (1.6 m tall bed of 0.053 m i.d), a loop-seal and the pressure control valves. The solid circulation rate was measured by varying the slide-gate opening positions, the gas velocities and temperatures of the desulfurizer and the voidage in the desulfurizer was derived by the same way. At the same gas velocities and the same opening positions of the slide gate, the solid circulation rate, which was similar at the temperature of $300^{\circ}C$ and $550^{\circ}C$, was low at those temperatures compared with a room temperature. The voidage in the desulfurizer showed a fast fluidized bed type when the opening positions of the slide gate were 10~20% while that showed a turbulent fluidized bed type when those of slide gate were 30~40%. The reaction characteristics of Zn-based solid sorbent were investigated by different desulfurization temperatures at 20 atm in the continuous operation. The $H_2S$ removal efficiency tended to decrease below the desulfurization temperature of $450^{\circ}C$. Thus, the 10 hour continuous operation has been performed at the desulfurization temperature of $500^{\circ}C$ in order to maintain the high $H_2S$ removal efficiency. During 10 hour continuous operation, the $H_2S$ removal efficiency was above 99.99% because the $H_2S$ concentration after desulfurization was not detected at the inlet $H_2S$ concentration of 5,000 ppmv condition using UV analyzers (Radas2) and the detector tube (GASTEC) which lower detection limit is 1 ppmv.

• 한국신재생에너지학회:학술대회논문집
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• 2009.06a
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• pp.871-872
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• 2009

본 연구에서는 석탄가스에 함유된 $H_2O/H_2S$ 농도변화에 따른 세가지 종류의 아연계 탈황제의 반응성능을 회분식 유동층반응기에서 분석하였다. 가스화에서 생성되는 가스의 조성은 모사가스를 이용하여 입구의 $H_2O$와 $H_2S$ 농도를 변화시켜 실험을 수행하였다. $H_2O$의 농도는 5%부터 30%까지 $H_2S$의 농도는 0.5%에서 2%로 변화시켜 탈황성능을 분석하였다. 실험 결과 $H_2O$의 농도가 증가할수록 탈황성능이 감소하였다. 입구의 $H_2S$ 농도가 증가할수록 탈황반응기 후단의 $H_2S$ 농도 역시 증가하였으나, 탈황성능은 최저 99.5%로 건식탈황제를 이용하여 99% 이상의 $H_2S$ 제거 성능을 보이는 것을 확인하였다.

• KSBB Journal
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• v.11 no.2
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• pp.238-245
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• 1996

Microbial desulfurization characterlstics of a bituminous coal have been determined by using Thiobacillus ferrooxidans. The effects of process variables (such as coal pulp density, particle size and addition of surfactants) on pyrite removal have been investigated in both shake and airlift-bioreactor culture experiments. In shake experiments, pyrite could be removed over 78% for pulp densifies below 20% (w/v) and removed below 40% for pulp densities over 30% (w/v) in 8 days. Pyrite removal decreased with increasing pulp densities, and it also decreased sharply with increasing particle sizes. In airlift bioreactor experiments, pyrite at 50% (w/v) pulp density could be removed about 50%. Its value is much higher than 15% at the same pulp density in a shake experiment. With addition of surfactants, pyrite removal was enhanced in shake experiments significantly, whereas it was slightly decreased in an airlift bioreactor experiment.