• Title/Summary/Keyword: 석탄 슬러리

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Effect of Operating Parameters on Microbial Desulfurization of Coal by Acidithiobacillus ferrooxidans. (Acidithiobacillus ferrooxidans에 의한 생물학적 석탄탈황에 미치는 조업인자의 영향)

    • Microbiology and Biotechnology Letters
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    • v.31 no.4
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    • pp.400-407
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    • 2003
  • In microbial coal desulfurization process (MCDP) by using Acidithiobacillus ferrooxidans, the effect of process variables on pyritic sulfur removal efficiency has been investigated. The inhibitory effect of toxic materials contained in coal matrix on the activity of desulfurizing bacteria have been evaluated in coal extracts, and the results showed that the method was useful to evaluate the applicability of a coal which is to be desulfurization to MCDP. The removal efficiency increased with decreasing particle size and decreases with increasing pulp density, but has no significant influence of particle size and pup densities at high pulp densities over 20 wt%. The mass transfers of gaseous nutrients such as oxygen and carbon dioxide into coal slurry with various pulp densities and coal particle size has been studied in an airlift bioreactor. Mass transfer coefficient was independent of pulp density in coal slurry with fine particle below 175 $\mu\textrm{m}$, but significantly decreased with increasing pulp density over 225 $\mu\textrm{m}$. The coal particles over 575 $\mu\textrm{m}$ were significantly settled to the bottom of bioreactor resulting in poor mixing. Considering mass transfer, pulp density and coal mixing, an optimal size of coal particle for the microbial coal desulfurization process seems to be about 500 $\mu\textrm{m}$.

Characteristics of Wet Feeding Gasification in an Entrained-flow Gasifier (습식 분류층 석탄가스화 운전 특성)

  • Ra, Ho-Won;Choi, Young-Chan;Yoon, Sang-Jun;Hong, Jai-Chang;Kim, Hae-Ho;Ra, Ho-Won;Kim, Jae-Ho;Lee, Jae-Goo
    • Proceedings of the KSME Conference
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    • 2008.11b
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    • pp.2953-2961
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    • 2008
  • 습식 석탄가스화란 석탄을 물과 혼합한 슬러리 형태(CWM, Coal Water Mixture)로 사용하는 것을 말하며, 분류층 가스화기에 빠르게 적용되었던 이유는 석유류 가스화와 공급방식이 유사하다는 점에서 출발하였다고 볼 수 있다. 1950년도에 사용되어 왔던 석유류 가스화 이용은 1970년 이후로는 유가 상승의 영향으로 석탄가스화로 바뀌게 되었다. 합성가스의 활용공정인 화학물질 제조 또는 복합발전의 운전 압력이 대부분 높기 때문에 가스화 압력을 높게 유지하기 위하여 슬러리 공급 방식이 많이 이용되었다. 슬러리 형태의 석탄 연료는 석유류가스와 시스템을 유사하게 활용할 수 있는 장점이 있으며, 특별히 고압을 필요로 하는 경우에도 비교적 간단한 시스템을 이용하여 공급 가능하다. 본 고에서는 현재까지 한국에너지기술연구원에서 수행된 습식 석탄가스화 기술개발 내용에 대하여 기술하고자 하였다.

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Ignition and combustion phenomena of a coal-water slurry droplet (석탄-물 슬러리 액적의 증발 및 점화현상 해석)

  • An, Guk-Yeong;Baek, Seung-Uk;Kim, Gwan-Tae
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.20 no.2
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    • pp.632-640
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    • 1996
  • The ignition and combustion characteristics of CWS droplets were investigated in the postflame region generated by a flat burner. The effect of radiation by screen and heating eleements ws taken into account. Also the theoretical claculations considering the temporal temeprature variation have been performed and compared with experimental results. The ignition delays were reduced by the radiation of the screen or heating elements. Therfore the radiation was considered to play some role in predicting the ignition delay.

The Effects of Surfactants on the Rheological Properties of Concentrated Coal-Water Slurry (고농도 석탄-물 슬러리계의 유변적 성질에 미치는 계면 활성제의 영향)

  • 서호준
    • The Korean Journal of Rheology
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    • v.9 no.1
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    • pp.1-5
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    • 1997
  • 새로이 합성한 계면확성제와 대표적 분산용 계면활성제의 분산효과를 상호 비교해 보기 위하여 고농도 석탄-물 슬러리계에 대한 유변학ㅈ거 성질을 측정하였다. 0~$25^{\circ}C$ 온도 범위에서 얻어진 유동곡선으로부터 여러 가지 유동 파라미터를 구한 결과, PS가 상대적으로 structure factor, C2와 shear modulus, $\chi$2/$\alpha$2 값에 있어서 큰 감소를 보여 주엇으며 특히 shear modulus는 계면활성제의 종류에 따라 큰차이를 보여주었다. 이러한 현상을 PS가 다 가음이곤 고분자 전해질과 유사한 구조를 갖고있어서 석탄 입자에 흡착시 입자간 정전기적 반발과 입체장애를 초래하여 슬러리의 유동성을 향상시킨데 따른 결과로 해석된다.

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Effect of Substituting Coal Fly Ash of Sawdust as a Bulking Agent for Swine Waste Composting (석탄회(石炭灰)(Coal fly ash)의 양돈분뇨처리(養豚糞尿處理) 부자재(副資材) 대체이용(代替利用)에 관(關)한 연구(硏究))

  • Chung, Hee-Sik;Seo, Jeoung-Yoon
    • Journal of the Korea Organic Resources Recycling Association
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    • v.7 no.1
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    • pp.43-52
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    • 1999
  • This study was carried out to investigate how much coal fly ash could be substituted for sawdust as a bulking agent for livestock waste composting. The mixtures of coal fly ash and sawdust in the weight ratio of 8 to 2, 7 to 3, 6 to 4, 5 to 5, 4 to 6, 3 to 7 and 2 to 8 were added to livestock waste as the bulking agent. The same amount of the bulking agents and livestock waste was mixed and composted during 21 days. Following effects were analyzed during composting experiment : the variation of temperature, pH and various compound contents. The results were summarized as follows: The more the sawdust was added, the higher the maximum temperature in slurry type livestock farm but faster it reached in scrapper type. Water content was maintained under good condition by adding the bulking agent mixed of the same amount of coal fly ash and sawdust. pH was in the range of 7~10 by adding the bulking agent mixed of the same amount of coal fly ash and sawdust. The more the sawdust was added, the higher organic matter content was measured. Nitrogen content with increasing the amount of sawdust added but it was higher did not showed any tendency Organic matter/Nitrogen ratio reduced during the composting period in scrapper type but it showed contrary tendency in slurry type with that of scrapper type.

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Atomization characteristics of burner nozzle for entrained flow gasifier (습식 석탄 가스화 장치에서 버너노즐에 따른 미립화 특성)

  • Ra, Ho-Won;Lee, Jae-Goo;Choi, Young-Chan;Yoon, Sang-Jun;Son, Young-Il;Hong, Jae-Chang
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.05a
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    • pp.353-355
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    • 2008
  • 최근 석탄 가스화 기술은 화석연료인 석탄을 기존의 공해물질 발생을 90%이상 줄이면서 고효율로 활용할 수 있는 방법으로 각광받고 있다. 본 연구는 습식 석탄 가스화기에서 가스화의 핵심적인 요소인 버너의 분무 관계 분야에 대한 분무 특성 및 무화성능을 높일 수 있는 분무기의 구조 및 운전 조건 등을 제시 할 목적으로 분무 시 내부를 관찰 할 수 있는 아크릴을 이용하여 내부 혼합식 버너를 제작하였다. 미립화 특성을 파악하기 위하여 $O_2$/Fuel Ratio 및 버너의 내부 혼합 방식, 분사각도, 각 분사 높이에 따른 미립화 특성을 관찰하였으며, 입도 분석은 심파텍사의 입도 분석기를 이용하여 측정하였다. 내부 혼합식 버너의 입도는 분사 각도와 $O_2$/Fuel Ratio에 따라서 변화하는 경향을 나타냈으며, 공급되어지는 Fuel은 석탄 슬러리와 물을 이용하여 각각의 입도를 측정하였다. slurry의 공급량이 고정된 상태에서 산소 공급량이 증가함에 따라 미립화도는 증가하는 경향을 나타내었으며, 슬러리 공급량과 산소 공급량이 동일한 경우 버너의 분사 각도에 따라 미립화도가 다르게 나타나는 특성을 관찰하였다.

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Economic Analysis of Upgrading Low Rank Coal Process (저등급석탄 고품위화 공정의 경제성 분석)

  • Chun, Dong-Hyuk;Kim, Sang-Do;Rhim, Young Joon;Lee, Si Hyun
    • Korean Chemical Engineering Research
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    • v.49 no.5
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    • pp.639-643
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    • 2011
  • Fry-drying of coal slurry is one of the upgrading low rank coal processes. It consists of slurry mixing, slurry dewatering, solvent recovery and briquetting. Cost estimation and economic feasibility are examined for the upgrading low rank coal process based on capacity of 1 million ton/yr. In case that investment costs are $100,000,000, discount rate is 12%, and service life is 20 years, the results of economic analysis are enough to satisfy the evaluation criteria of investment such as IRR, B/C ratio, NPV and discounted payback period. According to sensitivity analysis, investment value are very sensitive to raw material cost and product price. Since the bituminous coal price is currently soaring, it is expected that the investment value will increase more and more.

Desirable pH of Slurry in Desulfurization Absorber for a 1000 MW Coal Fired Power Plant (1000 MW급 석탄화력발전용 탈황흡수탑의 적정슬러리 pH)

  • Park, Jeong-kee;Yoo, Hoseon
    • Plant Journal
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    • v.15 no.1
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    • pp.38-44
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    • 2019
  • This research is an experimental investigation to find the desirable pH of slurry in the desulfurization absorber for a 1000 ㎿ coal fired power plant, operating in compliance with the Air Environmental Conservation Act and the plant's internal regulations. In case the average sulfur dioxide concentration in inflow flue gas, ${\bar{C\;in}}$ [ppm] changed to 500 ppm, 550 ppm, 600 ppm and 635 ppm after fixing inflow flue gas flow rate, generator output, pressure drop in the absorber, and oxidation air flow rate, the desirable pH of the slurry in the absorber, was 5.0, 5.2, 5.3 and 5.4. Thus, it is recommended that the desirable pH of slurry is calculated using the correlation equation, $RpH=0.0018{\times}{\bar{C\;in}}+4,2031$ when the average sulfur dioxide concentration in the inflow flue gas is in the range of 500 ppm to 635 ppm.