• Title/Summary/Keyword: 탄화수소 생성물

Search Result 106, Processing Time 0.051 seconds

Stenotrophomons maltophilia에 의한 방향족 화합물의 생분해

  • 최창석;박진희;김영식;이태진
    • Proceedings of the Korean Society of Soil and Groundwater Environment Conference
    • /
    • 2002.09a
    • /
    • pp.71-74
    • /
    • 2002
  • 다고리방향족 탄화수소를 페놀에 적응된 미생물을 이용하여 분해하고자 하였다. 분리된 Stenotrophomons maltophilia는 나프탈렌과 페난스렌을 탄소원 및 에너지원으로 이용하였으며 10mg/$\ell$의 나프탈렌과 0.9mg/$\ell$의 페난스렌이 완전히 분해되는데 지체기후 약 2일과 3일이 소요되었다. 나프탈렌, 페난스렌의 분해시 중간생성물로 chromatography 상에 새로운 피크들이 생성되었으며, 이러한 중간생성물을 파악하여 다고리 방향족 탄화수소의 분해경로를 모색하고자 하였다.

  • PDF

Biodegradation of PAHs in anaerobic conditions

  • 우승한;임경희;박종문
    • Proceedings of the Korean Society of Soil and Groundwater Environment Conference
    • /
    • 2004.04a
    • /
    • pp.153-157
    • /
    • 2004
  • 다양한 혐기성 조건에서 다환방향족탄화수소(PAHs)로 오염된 토양의 미생물 분해 연구를 수행하였다. 대표적인 다환방향족탄화수소인 phenanthrene과 fluorene을 토양과 물에 오염시켜서 약 100일 동안 저감정도를 관찰하였고, 실제 다환방향족탄화수소로 오염된 현장 토양을 이용 혐기성하에서 다환방향족탄화수소의 생분해 가능성을 확인하였다. 미생물 접종원은 혐기성 조건에서 다환방향족탄화수소에 노출시킨 슬러리가 사용되었다. 황산염 환원조건, 질산염 환원조건, 메탄생성조건 등의 다양한 혐기성 조건에서 실험을 수행한 결과, 메탄생성조건 > 질산염 환원조건 > 황산염 환원조건의 순서로 분해가 잘 일어났다. 또한 현장오염토양의 경우 34일간 처리 후 메탄생성조건에서 최대 72%의 분해율을 보였다.

  • PDF

Mechanism of Methanol Conversion over Zeolite and Molecular Sieve Catalysts (제올라이트와 분자체 촉매에서 메탄올 전환 반응의 기구)

  • Seo, Gon;Min, Byung Goo
    • Korean Chemical Engineering Research
    • /
    • v.44 no.4
    • /
    • pp.329-339
    • /
    • 2006
  • The production of lower olefins from methanol becomes an attractive process because of the rapid increase in crude oil price. This paper reivews the conversion mechanisms of methanol to hydrocarbons over zeolite and SAPO molecular sieve catalysts to understand the formation steps of lower olefins from methanol. The feasibility of the conversion mechanisms such as the direct mechanism based on well-defined intermediates and the hydrocarbon pool mechanism involving hydrocarbon moieties as an active centers is discussed with reepect to the induction period, the selectivity for products and the deactivation phenomena of the methanol conversion. The literature appeered since 1999 for the structure of the hydrocarbon pool and its catalytic role in the methanol conversion are summariged, and the prospect for the methanol-to-olefins process is described.

Hydrogenation of Polycyclic Aromatic Hydrocarbons Over Pt/Kieselguhr Catalysts in a Trickle Bed Reactor (Trickle Bed Reactor에서 Pt/Kieselguhr 촉매를 이용한 다환방향족 탄화수소 수소화 반응)

  • Seung Kyo, Oh;Seohyeon, Oh;Gi Bo, Han;Byunghun, Jeong;Jong-Ki, Jeon
    • Clean Technology
    • /
    • v.28 no.4
    • /
    • pp.331-338
    • /
    • 2022
  • The objective of this study is to prepare bead-type and pellet-type Pt (1 wt%)/Kieselguhr catalysts as hydrogenation catalysts for the polycyclic aromatic hydrocarbons (PAHs) included in pyrolysis fuel oil (PFO). The optimal reaction temperature to maximize the yield of saturated cyclic hydrocarbons during the PFO-cut hydrogenation reaction in a trickle bed reactor was determined to be 250 ℃. A hydrogen/PFO-cut flow rate ratio of 1800 was found to maximize 1-ring saturated cyclic compounds. The yield of saturated cyclic compound increased as the space velocity (LHSV) of PFO-cut decreased. The difference in hydrogenation reaction performance between the pellet catalyst and the bead catalyst was negligible. However, the catalyst impregnated by Pt after molding the Kieselguhr support (AI catalyst) showed higher hydrogenation activity than the catalyst molded after Pt impregnation on the Kieselguhr powder (BI catalyst), which was a common phenomenon in both the pellet catalysts and bead catalysts. This may be due to a higher number of active sites over the AI catalyst compared to the BI catalyst. It was confirmed that the pellet catalyst prepared by the AI method had the best reaction activity of the prepared catalysts in this study. The majority of the PFO-cut hydrogenation products were cyclic hydrocarbons ranging from C8 to C15, and C11 cyclic hydrocarbons had the highest distribution. It was confirmed that both a cracking reaction and hydrogenation occurred, which shifted the carbon number distribution towards light hydrocarbons.

Study on the decomposition of 1,1,2-trichloroethane in a pyrolysis reactor and a numerical study for scale-up design (열분해 반응기에서 1,1,2-trichloroethane의 분해특성과 Scale-up 설계를 위한 수치해석적 연구)

  • 이채복;라승혁;강경태;김상용
    • Proceedings of the Korea Air Pollution Research Association Conference
    • /
    • 2002.11a
    • /
    • pp.417-418
    • /
    • 2002
  • 열분해는 독성이 강한 염화탄화수소의 처리뿐만 아니라 염화물을 효과적으로 제거하여 이들로부터 유용한 탄화수소를 얻을 수 있는 반응이다 Biomass에 열분해를 적용하여 가스상, 액상, 고상형태의 유동한 부산물로 전환시키고 있으며 현재 액상생성물은 외국에서 큰 주목을 받고 있는 부산물이다. 1,1,2-trichloroethane(TCE)는 독성이 강한 휘발성 유기화합물(VOC)이며 발암물질이다. (중략)

  • PDF