Molecular reconstruction of naphtha steam cracking feedstocks based on commercial indices

نویسندگان

  • Kevin M. Van Geem
  • Damien Hudebine
  • Marie Françoise Reyniers
  • François Wahl
  • Jan J. Verstraete
  • Guy B. Marin
چکیده

A new method for feedstock reconstruction of industrially important hydrocarbon fractions is developed using as input the analytically determined ommercial indices such as the average molecular weight, the specific density, theH/C-ratio, the paraffin, isoparaffin, olefins, naphthenes, aromatics PIONA) weight fractions and a set of ASTM boiling points. The method is based on Shannon’s entropy criterion and allows generating a molecular omposition of a naphtha fraction that meets all the boundary conditions set by the industrially available commercial indices. The most important omponents present in a naphtha fraction are selected as possible feedstock components. This approach is very fast because the optimization unction can be transformed from a nonlinear equation in the N mole fractions (N∼ 102) into a nonlinear equation in maximally 14 parameters, aking it very attractive for the petrochemical industry. A good correspondence exists between the simulated weight fractions and the actual nalytically determined ones provided that the specified commercial indices are sufficiently accurate. The feedstock module is implemented in a imulation package for steam cracking but can be used as a stand-alone tool too. The combination of these two simulation tools makes it possible to btain a good agreement between the simulated and experimentally determined product yields for a set of 50 pilot plant experiments with different aphtha feedstocks under widely varying operating conditions. 2006 Elsevier Ltd. All rights reserved.

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

ثبت نام

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

منابع مشابه

SHAHAB-A PC-Based Software for Simulation of Steam Cracking Furnaces (Ethane and Naphtha)

SHAHAB is a PC- based simulator developed by Olefin Research Group (ORG), with the simultaneous simulation of the reactor, the firebox, the convection section and the transfer line exchanger in steam Cracking units. The reaction mechanism of thermal cracking of hydrocarbons is generally accepted as free-radical chain reactions. Using a rigorous kinetic model, a complete reaction network for rep...

متن کامل

Modeling and Simulation for Olefin Production in Amir Kabir Petrochemical

Abstract — The Ethylene production process is one of the most important aspects of a petrochemical plant. The bulk of the worldwide annual commercial production of Ethylene is based on thermal cracking of petroleum hydrocarbons with steam. This process is commonly called Steam cracking process. This article deals with Amir Kabir Petrochemical Olefin Furnaces that are located in special region o...

متن کامل

Simulation and Optimization of a Naphtha Thermal Cracking Pilot Plant

In thermal cracking plants, it is desired to apply an optimal temperature profile along the reactor to minimize the operation cost. In this article a simulator is developed by the use of a mathematical model, which describes the static operation of a naphtha thermal cracking pilot plant. The model is used to predict the steady state profiles of the gas temperature and product yields. Using ...

متن کامل

Wood-derived olefins by steam cracking of hydrodeoxygenated tall oils.

Tall oil fractions obtained from Norwegian spruce pulping were hydrodeoxygenated (HDO) at pilot scale using a commercial NiMo hydrotreating catalyst. Comprehensive two dimensional gas chromatography (GC×GC) showed that HDO of both tall oil fatty acids (TOFA) and distilled tall oil (DTO) produced highly paraffinic hydrocarbon liquids. The hydrotreated fractions also contained fatty acid methyl e...

متن کامل

Energy Efficiency and Innovative Emerging Technologies for Olefin Production

Among the current IPPC installations, steam cracking for olefin production is the single most energy consuming process (ca. 30%) in the chemical industry, accounting for ca. 180 million tons of CO2 worldwide. This paper reviews steam cracking and innovative emerging olefin technologies in terms of energy efficiency. Pyrolysis section alone consumes ca. 65% of the total energy use and ca. 75% of...

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

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

ثبت نام

اگر عضو سایت هستید لطفا وارد حساب کاربری خود شوید

عنوان ژورنال:
  • Computers & Chemical Engineering

دوره 31  شماره 

صفحات  -

تاریخ انتشار 2007