Ethylene Yield from Pyrolysis Cracking in Olefin Plant Utilizing Regression Analysis

نویسندگان

چکیده

Ethylene yield is significant in showing the performance of steam cracker furnace olefin plant. This study was conducted actual large-scale plant to see impact various variables towards ethylene yield. The analysis utilizing Regression Analysis Minitab Software Version 18 develop a reliable model. model concluded that studied contributed by factor -0.000901, 0.02649, -0.282, 0.16, -0.0834, 0.1268, and 0.0057 Hearth Burner Flow, Integral Steam Drum Pressure, Super High-Pressure (SHP) Boiler Feed Water SHP Naphtha Stack NOx Emission respectively. Response Optimizer tool also showed from naphtha liquid feed pyrolysis cracking can be maximized at 32.55% with control setting 9,476.41 kg/hr 608.56 112.93 Barg 109.11 t/hr 86.42 63.49 Flow 126.23 mg/m 3 Emission.

برای دانلود باید عضویت طلایی داشته باشید

برای دانلود متن کامل این مقاله و بیش از 32 میلیون مقاله دیگر ابتدا ثبت نام کنید

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

منابع مشابه

Olefin production from catalytic cracking of light fuel oil over different additives

The catalytic cracking of a fuel oil over fluid catalytic cracking (FCC) catalyst has been investigated applying different additives. Catalyst mixtures consisting of a equilibrium FCC catalyst (E-Cat) blended with ZSM-5, MCM-41 and Mordenite additives were examined at the additive levels of 25 wt.%. The catalytic performance of the matrix was studied in a fixed bed micro-activity test unit (MAT...

متن کامل

Olefin Production from Heavy Liquid Hydrocarbon Thermal Cracking: Kinetics and Product Distribution

Thermal cracking of a heavy liquid hydrocarbon was performed in a laboratory scale tubular reactor. Central Composite Design (CCD), was used as an experimental design method. The design variables were Coil Outlet Temperature (COT), feed flow and rate steam ratio. Maximum yield of ethylene was 30.37 wt% at COT, residence time and steam ratio of 869oC, 0.208 s and 1.22 g/g, respect...

متن کامل

Olefin production from catalytic cracking of light fuel oil over different additives

The catalytic cracking of a fuel oil over fluid catalytic cracking (FCC) catalyst has been investigated applying different additives. Catalyst mixtures consisting of a equilibrium FCC catalyst (E-Cat) blended with ZSM-5, MCM-41 and Mordenite additives were examined at the additive levels of 25 wt.%. The catalytic performance of the matrix was studied in a fixed bed micro-activity test unit (MAT...

متن کامل

Thermodynamic Analysis of Light Olefins Production via Cracking of n-Hexane Using Gibbs Energy Minimization Approach and Analysis of Overall Reactions

Thermodynamic analysis of the cracking of hexane has been conducted by the Gibbs free energy minimization method and second law analysis of overall reactions. By-products have been divided into three groups of methane, alkynes and aromatics and their possible production paths have been discussed. Effect of operating conditions such as temperature and steam-to-hexane ratio on the cracking perfor...

متن کامل

olefin production from catalytic cracking of light fuel oil over different additives

the catalytic cracking of a fuel oil over fluid catalytic cracking (fcc) catalyst has been investigated applying different additives. catalyst mixtures consisting of a equilibrium fcc catalyst (e-cat) blended with zsm-5, mcm-41 and mordenite additives were examined at the additive levels of 25 wt.%. the catalytic performance of the matrix was studied in a fixed bed micro-activity test unit (mat...

متن کامل

ذخیره در منابع من


  با ذخیره ی این منبع در منابع من، دسترسی به آن را برای استفاده های بعدی آسان تر کنید

ژورنال

عنوان ژورنال: E3S web of conferences

سال: 2021

ISSN: ['2555-0403', '2267-1242']

DOI: https://doi.org/10.1051/e3sconf/202128703004