• Title/Summary/Keyword: 나프타 분해

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촉매이용 나프타 분해공정 상용화에 성공

  • Park, Yong-Gi
    • The Science & Technology
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    • s.501
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    • pp.46-49
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    • 2011
  • 나프타분해기술이란 석유화학산업의 기초 원료인 경질올레핀(에틸렌, 프로필렌)을 생산하기 위한 기술로서 철강산업에서 제철산업이 하는 역할을 화학산업에서 한다고 볼 수 있다. 즉, 각종 합성수지 및 화학제품을 생산하기 위한 기초화학원료를 만드는 기술이다.

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Comparison Analysis on Characteristics and Components of Various Waste Plastic Pyrolysis Oils by Vacuum Distillation Method (감압증류를 통해 분획된 폐플라스틱 열분해유의 특성평가와 구성성분 비교분석 연구)

  • Hwayeon Jeon;Cheol Hwan Jeon;Sung Joon Park;Jae Woo Lee;Jae-kon Kim
    • Clean Technology
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    • v.29 no.4
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    • pp.262-271
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    • 2023
  • Globally, the amount of waste plastics has been occurring to environmental problems. As a result, it is necessary to research methods that utilize waste plastic pyrolysis oil (WPPO) produced by pyrolysis. One such method being studied is utilizing WPPO as a naphtha feedstock. In this study, five types of WPPO were analyzed to determine whether they can be used as raw materials for naphtha. Because of their wide boiling point range, the WPPOs were fractionated into light and heavy fractions through vacuum distillation, and the separation and purification techniques were analyzed using GC-VUV to determine the content of paraffin, olefin, and other compounds. All WPPOs showed high olefin content regardless of the source and fraction. Aromatic and paraffin content varied depending on the source, and oxygen and other compounds also varied significantly by source and fraction. In addition, the light fraction showed a carbon distribution similar to that of naphtha, whereas the heavy fraction showed a carbon distribution of C11 ~ C14. In conclusion, additional processes and raw material selection are required to utilize waste plastic pyrolysis oil as a raw material for naphtha.

Synthesis of Carbon Materials from PFO, Byproducts of Naphtha Cracking Process (나프타 분해공정 부산물인 PFO로부터 탄소구조체 합성)

  • Lee, Jiyon;Park, Seung-Kyu
    • Applied Chemistry for Engineering
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    • v.22 no.5
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    • pp.495-500
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    • 2011
  • Separation of naphthalene from pyrolyzed fuel oil, by product of Naphta cracking process (NCC) process, has been accomplished by the solvent extraction, distillation and purification process. The residual pyrolyzed fuel oil (PFO), called precursor of carbon materials, has been calcined at $300{\sim}800^{\circ}C$ in nitrogen gas to raw pitch. After the treatment of PFO by hexane and methanol, either a flake phased carbon at $350^{\circ}C$ or a carbon sphere at above $400^{\circ}C$ forms. As the calcination temperature increases, the shape of raw pitch changes from the flake phase to the sphere one, and the size of them decreases to several ${\mu}m$. Based on the BET and XRD spectrum, the carbon sphere is classified to a mesophase amorphous carbon with a cubic phase.

Study of Pyrolysis Behavior of Alberta Oil Sand by Continuous Operation of Fluidized-Bed Reactor (Alberta 오일샌드의 유동층 열분해 연속실험을 통한 열분해 특성 파악)

  • Shin, Jong-Seon;Sun, Yang Kuk;Park, Young Cheol;Bae, Dal-Hee;Jo, Sung-Ho;Shun, Dowon
    • Korean Chemical Engineering Research
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    • v.48 no.1
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    • pp.68-74
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    • 2010
  • In this study, fluidized-bed pyrolysis has been conducted in order to recover the bitumen contained in the oil sand. Canada Alberta oil sand contains 11.9% of bitumen and the bitumen-derived heavy oil produced in fluidizedbed tends to be upgraded relative to the bitumen. The continuous operation has been performed using $N_2$ as a fluidization gas at 1 atm and $500^{\circ}C$ in a reactor of 170 cm height. The results showed 87.76% of bitumen conversion, where liquid products are 74.45% and gas products are 13.31%. $H_2$, $O_2$, CO, $CO_2$, $CH_4$, and NO and $C_1{\sim}C_4$ hydrocarbons in the gas products were analyzed by on-line gas analyzer and gas chromatography, respectively. The pyrolysis oil was analyzed by using proximate analysis, heavy metal analysis, SIMDIS, asphaltenes, and heating value. By SIMDIS analysis, naphtha was 11.50%, middle distillation was 44.83% and heavy oil was 43.66%. It was obvious that the pyrolysis oil was upgraded compared with bitumens.

Fault-consequence digraph를 이용한 전문가 시스템의 지식베이스 구현

  • 윤병석;오전근;윤인섭
    • 제어로봇시스템학회:학술대회논문집
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    • 1989.10a
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    • pp.389-394
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    • 1989
  • 본 연구에서는 화학공정의 자동화와 관련된 실시간 나프타 분해로 이상진단 시스템의 한 부분을 구성하고 있는 지식기반의 구현을 위하여 공정변수 상호간의 관계를 나타낸 signed directed graph(SDG)를 기반으로 이상에서 파급되는 증상들을 순서대로 나타내는 fault-consequence digraph(FCD)를 지식모델로 사용했고, 이를 사고사례를 이용하여 검토해본 결과 초기에 정확한 이상원인 후보를 찾아내므로써 이상진단 전문가 시스템의 지식모델로 적합함을 알 수 있었다.

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The Consequence Analysis for Fire Accidents by the Continuous Release of Butane Vapor in the Debutanizing Process of Naphtha Cracking Plant (나프타분해플랜트의 부탄추출공정에서 부탄증기의 연속누출에 의한 화재사고의 영향평가)

  • 윤대건;이헌창;함병호;조지훈;김태옥
    • Fire Science and Engineering
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    • v.12 no.2
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    • pp.3-15
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    • 1998
  • The consequence analysis for jet and flash fire accidents by the continuous release of butane vapor was performed and effects of process variables on consequences were analyzed in standard conditions. For the continuous release (87.8 kg/s) of butane vapor at 8m elevated height in the debutanizing process of the naphtha cracking plant operating at 877 kPa, 346.75 K, we found that for the jet fire accident, shape and size of the flame could be predicted and thermal radiation estimated by API model at 200m distance from release point was 1.5kW/$m^2$, and that for the flash fire accident, effect range was 11.2~120.2m. Also, simulation results showed that effects of operating pressures on consequences were larger than those of operating temperatures and results of accidents were increased with increasing operating pressures. At this time, effects of operating pressures on XUFL were smaller(about 1/10) than those on XLFL for the flash fire accident.

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Well-to-Wheel Greenhouse Gas Emissions Analysis of Hydrogen Fuel Cell Vehicle - Hydrogen Produced by Naphtha Cracking (나프타 기반 수소 연료전지 자동차의 전과정 온실가스 발생량 분석)

  • Kim, Myoungsoo;Yoo, Eunji;Song, Han Ho
    • Transactions of the Korean Society of Automotive Engineers
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    • v.25 no.2
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    • pp.157-166
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    • 2017
  • The Fuel Cell Electric Vehicle(FCEV) is recently evolving into a new trend in the automobile industry due to its relatively higher efficiency and zero greenhouse gas(GHG) emission in the tailpipe, as compared to that of the conventional internal combustion engine vehicles. However, it is important to analyze the whole process of the hydrogen's life cycle(from extraction of feedstock to vehicle operation) in order to evaluate the environmental impact of introducing FCEV upon recognizing that the hydrogen fuel, which is used in the fuel cell stack, is not directly available from nature, but instead, it should be produced from naturally available resources. Among the various hydrogen production methods, ${\sim}54.1%^{8)}$ of marketed hydrogen in Korea is produced from naphtha cracking process in the petrochemical industry. Therefore, in this study, we performed a well-to-wheels(WTW) analysis on the hydrogen fuel cycle for the FCEV application by using the GREET program from the US Argonne National Laboratory with Korean specific data. As a result, the well-to-tank and well-to-wheel GHG emissions of the FCEV are calculated as 45,638-51,472 g $CO_2eq/GJ$ and 65.0-73.4 g $CO_2eq/km$, respectively

Synthesis of Pitch from PFO, Byproduct of Naphtha Cracking Process Using UV Irradiation and AlCl3 Catalyst (나프타 분해공정 부산물인 PFO로부터 UV 조사와 AlCl3 촉매 첨가를 이용한 피치의 합성)

  • Jung, Min-Jung;Ko, Yoonyoung;Lee, Young-Seak
    • Applied Chemistry for Engineering
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    • v.26 no.2
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    • pp.224-228
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    • 2015
  • The carbon precursor pitch from pyrolyzed fuel oil (PFO), by-product of Naphta cracking process (NCC), was prepared through heat and UV irradiation treatments with various concentrations of $AlCl_3$, which is a new pitch preparation method. The reformed pitches were characterized by measuring their elemental composition, chemical structure of components, molecular weight distribution, and softening point. The oxygen contents of reformed pitch increased as increasing $AlCl_3$ amounts on the other hand, the carbon and hydrogen contents were not nearly changed. UV irradiated reformed pitches were composed of more aromatic carbon compounds than that of using only heat-treatment without any UV irradiation. The addition of $AlCl_3$ catalyst was ineffective on the aromaticity of reformed pitches. The softening point of prepared pitches was in the range of $103.3{\sim}168.9^{\circ}C$. Also the yield of prepared pitch increased from 48% to 80% when 5 wt% of $AlCl_3$ was added during the heat and UV irradiation reforming. It is expected that the UV irradiation reforming method can be practical and helpful to produce high yields of pitches with diverse properties.

The Consequence Analysis for Unconfined Vapor Cloud Explosion Accident by the Continuous Release of Butane Vapor in the Debutanizing Process of Naphtha Cracking Plant (나프타분해플랜트의 부탄추출공정에서 부탄증기의 연속누출에 의한 증기운 폭발사고의 영향평가)

  • 손민일;이헌창;장서일;김태옥
    • Journal of the Korea Safety Management & Science
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    • v.2 no.4
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    • pp.33-43
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    • 2000
  • The consequence analysis for the unconfined vapor cloud explosion(UVCE) accident by the continuous release of butane vapor was performed and effects of process parameters on consequences were analyzed in standard conditions. For the case of continuous release(87.8 kg/s) of butane vapor at 8 m elevated height in the debutanizing process of tile naphtha cracking plant operating at 877 kPa & 346.75 K, we found that combustion ranges of dispersed vapor estimated by HMP model were 11.2~120.2 m and overpressures estimated by TNT equivalency model at 200 m were about 37.35~55.1 kPa. Also, overpressures estimated by Model UVCE I based on advective travel time to $X_{LFL}$ were smaller than those estimated by Model UVCE IIbased on real travel time between $X_{UFL}$ and $X_{LFL}$. At the same time, damage intensities at 200 m and effect ranges by overpressure could be predicted. Furthermore, simulation results showed that effects of operating pressures on consequences were larger than those of operating temperatures and results of accidents were increased with increasing operating pressures. At this time, sensitivities of overpressures for UVCE accident by the continuous release were about 5 kPa/atm.

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