• 제목/요약/키워드: Coke

검색결과 274건 처리시간 0.013초

석유 코크스의 에너지 전환 : CO2 가스화 (Energy conversion of petroleum coke : CO2 gasification)

  • 국진우;곽인섭;이시훈
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2014년도 제49회 KOSCO SYMPOSIUM 초록집
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    • pp.255-257
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    • 2014
  • The installation of light oil facilities or delayed cokers seems to be inevitable in the oil refinery industry due to the heavy crude oil reserves and the increased use of light fuels as petroleum products. Petroleum coke is a byproduct of oil refineries and it has higher fixed carbon content, higher calorific value, and lower ash content than coal. However, its sulfur content and heavy metal content are higher than coal. In spite of disadvantages, petroleum coke might be one of promising resources due to gasification processes. The gasification of petroleum coke can improve economic value of oil refinery industries by handling cheap, toxic wastes in an environment-friendly way. In this study, $CO_2$ gasification reaction kinetics of petroleum coke, various coals and mixing coal with petroleum coke have investigated and been compared by using TGA. The kinetics of $CO_2$ gasification has been performed with petroleum coke, 3 kinds of bituminous coal [BENGALLA, White Haven, TALDINSKY], and 3 kinds of sub-bituminous coal [KPU, LG, MSJ] at various temperature[$1100-1400^{\circ}C$].

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니켈 촉매를 이용한 프로판 예개질 반응의 탄소침적에 대한 연구 (Carbon Deposition on Nickel Catalyst for Pre-reforming of Propane)

  • 김선영;배중면
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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    • pp.487-490
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    • 2008
  • Temperature programmed oxidation (TPO) is used to characterize coke species deposited on commercial nickel catalyst, C11-PR during propane pre-reforming. Propane pre-reforming performed under various condition, S/C from 1.5 to 2.5 and temperature from $350^{\circ}C$ to $450^{\circ}C$. There are three kinds of coke species detected by TPO: (i) reactive coke, (ii) coke deposited on metal site and (iii) coke deposited on acid support. Coke deposited on metal and support are minimized although reactive coke is generated at temperature of $400^{\circ}C$ and S/C of 2.0. Reactive coke is expected to remove easily below temperature of $200^{\circ}C$. Therefore, optimized pre-reforming condition for propane is $400^{\circ}C$ and S/C of 2.0.

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스왐기반 퍼지시스템을 이용한 코크오븐 연소제어 모델링 (A combustion control modeling of coke oven by Swarm-based fuzzy system)

  • 고언태;황석균;이진수
    • 대한전기학회:학술대회논문집
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    • 대한전기학회 2005년도 학술대회 논문집 정보 및 제어부문
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    • pp.493-495
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    • 2005
  • This paper proposes a swarm-based fuzzy system modeling technique for coke oven combustion control diagnosis. The coke plant produces coke for the blast furnace plant in steel making process by charging coal into oven and supplying gas to carbonize it. A conventional mathematical model for coke oven combustion control has been used to control the amount of gas input, but it does not work well because of highly nonlinear feature of coke plant. To solve this problem, swarm-based fuzzy system modeling technique is suggested to construct a diagnosis model of coke oven combustion control. Based on the measured input-output data pairs, the fuzzy rules are generated and the parameters are tuned by the PSO(Particle Swarm Optimizer) to increase the accuracy of the fuzzy system is operated. This system computes the proper amount of gas input taking the operation conditions of coke oven into account, and compares the computed result with the supplied gas input.

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프로판 탈수소화 반응용 백금촉매의 코크 생성에 미치는 수소비와 주석첨가의 영향 (Effect of Hydrogen Ratio and Tin Addition on the Coke Formation of Platinum Catalyst for Propane Dehydrogenation Reaction)

  • 김수영;김가희;고형림
    • 청정기술
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    • 제22권2호
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    • pp.82-88
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    • 2016
  • 코크에 의한 촉매의 불활성화는 산업현장에서 촉매가 사용되는 동안 매우 중요하다. 본 연구에서는 프로판 탈수소 반응을 위한 Pt-Sn 촉매에서 반응조건인 수소의 비율이 코크생성에 미치는 영향과 코크버닝에 의한 촉매 활성의 회복여부, 그리고 코크양에 따른 코크버닝 중의 백금소결여부, Pt-Sn-K 촉매에서 Sn의 함량이 코크생성과 불활성화에 미치는 영향을 확인하고자 하였다. Pt-Sn-K는 Pt와 Sn, K를 순차적으로 각각 θ-알루미나와 γ-알루미나에 담지 하여 제조하였다. 프로판 탈수소 반응은 먼저 반응물중의 수소비를 달리하여 620 ℃에서 수행한 후, 코크버닝을 통해 재생하고 다시 프로판 탈수소 성능을 비교하였다. 재생촉매의 B.E.T 분석과 코크분석, XRD (X-ray diffraction)와 같은 물리분석을 동시에 수행하였다. 촉매의 활성테스트와 특성분석을 통하여 반응물 상에서 수소의 비와 촉매의 Sn함량이 촉매표면의 코크 형성에 영향을 줄 수 있다는 것을 알 수 있다. 또한, 과량의 코크는 Air 재생 과정에서의 백금입자의 소결을 일으키고 촉매의 활성을 저하시킬 수 있다.

영상인식을 이용한 이동기기 정 중심확인 시스템 개발 (Development of center position control system for travelling machines using image processing)

  • 최일섭;전종학
    • 제어로봇시스템학회:학술대회논문집
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    • 제어로봇시스템학회 1996년도 한국자동제어학술회의논문집(국내학술편); 포항공과대학교, 포항; 24-26 Oct. 1996
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    • pp.1484-1487
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    • 1996
  • An Automatic coking control system was developed to achieved substantial energy and labor savings through the stabilization and optimization of coke oven operation. With the aim of saving energy and labor, the coke department has been advanced automation and systematization. A typical examples of automation is Center Position Control System(CPCS) for coke oven. This system is proved effective in improvement of center position accuracy.

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탄소재 제조에 있어서 Raw Coke의 전처리의 영향 (Influence by Preheat-Treatment on Raw Coke in Fabrication of Carbon Solids)

  • 염희남;황인수;이종민;정윤중
    • 한국세라믹학회지
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    • 제31권1호
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    • pp.97-103
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    • 1994
  • The influence of ground petroleum coke, preheat-treated at temperatures ranged of 150~35$0^{\circ}C$, was studied. It has been found that the coke powder preheat-treated at the temperature of 175$^{\circ}C$ has been spherical-shaped in grinding and have showed the highest strength and density in sintering. The coke powder was also the best for the binding force and the (H/C) values showed 0.45 at the above temperature.

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Raw Coke의 하소온도에 따른 구조변화 (Structural Changes During the Calcination of Raw Coke)

  • 염희남;장진석;이종민;정윤중
    • 한국세라믹학회지
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    • 제29권10호
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    • pp.773-778
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    • 1992
  • The effect of temperature on the structural changes of petroleum raw coke during calcination was studied and then the properties of carbon solids prepared from those calcined coke using binder were examined. The notable structural change of raw coke was observed in the range from 800$^{\circ}C$ to 900$^{\circ}C$ from the results of volatile matter, porosity, X-ray diffraction and scanning electron microscopy. The bending strength, density of the carbon solid carbonized at 1400$^{\circ}C$ was 400 kg/$\textrm{cm}^2$ and 1.40g/㎤, respectively.

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New insights about coke deposition in methanol-to-DME reaction over MOR-, MFI- and FER-type zeolites

  • Migliori, Massimo;Catizzone, Enrico;Aloise, Alfredo;Bonura, Giuseppe;Gomez-Hortiguela, Luis;Frusteri, Leone;Cannilla, Catia;Frusteri, Francesco;Giordano, Girolamo
    • Journal of Industrial and Engineering Chemistry
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    • 제68권
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    • pp.196-208
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    • 2018
  • The effect of channel-system of zeolite on methanol-to-DME reaction was studied. Results revealed that channels size and topology affect catalyst lifetime, type and location of coke precursors. FER and MFI showed the best resistance towards coke deposition, whilst fast deactivation was observed on MOR. Although the higher concentration and strength of acid sites, FER structure formed a lower coke amount, preferably located within the pores, while coke cluster deposited on the external surface of MOR. Analysis of acid sites distribution and strength was performed during deactivation-regeneration process. Coke location assessment was also supported by molecular simulations.

FUNDAMENTAL UNDERSTANDING OF CRACKING AND BULGING IN COKE DRUMS

  • Penso, Jorge;Tsai, Chon
    • 대한용접접합학회:학술대회논문집
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    • 대한용접접합학회 2002년도 Proceedings of the International Welding/Joining Conference-Korea
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    • pp.675-680
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    • 2002
  • Cracking and bulging in welded and internally lined pressure vessels that work in thermal-mechanical cycling service have been well known problems in the petrochemical, power and nuclear industries. However, published literature and industry surveys show that similar problems have been occurring during the last 50 years. A better understanding of the causes of cracking and bulging causes is needed to improve the reliability of these pressure vessels. This study attempts to add information required for increasing the knowledge and fundamental understanding required. Typical examples of this problem are the coke drums in the delayed coking units refinery process. This case was selected for experimental work, field study and results comparison. Delayed coking units are among the refinery units that have higher economical yields. To shut down these units represents a high negative economical impact in refinery operations. Also, the maintenance costs associated with repairs are commonly very high. Cracking and bulging occurrences in the coke drums, most often at the weld areas, characterize the history of the operation of delayed coking units. To design and operate more robust coke drums with fewer problems, an improved metallurgical understanding of the cracking and bulging mechanisms is required. A methodology that is based field experience revision and metallurgical analyses for the screening of the most important variables, and subsequent finite element analyses to verify hypotheses and to rank the variables according to their impact on the coke drum lives has been developed. This indicated approach provides useful information for increasing coke drum reliability. The results of this work not only order the most important variables according to their impact in the life of the vessels, but also permit estimation of the life spans of coke drums. In conclusion, the current work shows that coke drums may fail as a combination of thermal fatigue and other degradation mechanisms such as: corrosion at high and low temperatures, detrimental metallurgical transformations and plastic deformation. It was also found that FEA is a very valuable tool for understanding cracking and bulging mechanisms in these services and for ranking the design, fabrication, operation and maintenance variables that affect coke drum reliability.

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주물용 코우크스와 무연괴탄의 가스화 반응과 강도에 관한 연구 (A Study on Gasification Reaction and Strength of Foundry Coke and Lump Anthracite Coal)

  • 조남돈;김종훈
    • 한국주조공학회지
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    • 제9권3호
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    • pp.247-256
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    • 1989
  • The gasification reaction rates by $CO_2$ in $CO/CO_2/N_2$ of various compositions in the temperature range of $900-1200^{\circ}C$ were measured for foundry coke and anthracite lump. The data for the rates was analyzed with Langmuir-Hinshelwood rate equations for the gasification of carbonaceous specimens. The values of the apparent activation energies of the reactions obtained from these data were ranged to be 47-99 and 73-128Kcal/mol respectively for foundry coke and for anthracite lump. The major contribution to decrease in tensile strength was shown to be attributable to the enlarging of the macropores in the coke and that of crack in the anthracite lump. Under the same experiment of the gasification of foundry coke, the rate of form coke was increasing as the addition of $Fe_2O_3$ increases.

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