Polycyclic Aromatic Hydrocarbons and Petroleum Industry
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Naphtha Catalytic Cracking Process Economics Program Report 29K
` IHS CHEMICAL Naphtha Catalytic Cracking Process Economics Program Report 29K December 2017 ihs.com PEP Report 29K Naphtha Catalytic Cracking Michael Arne Research Director, Emerging Technologies IHS Chemical | PEP Report 29K Naphtha Catalytic Cracking PEP Report 29K Naphtha Catalytic Cracking Michael Arne, Research Director, Emerging Technologies Abstract Ethylene is the world’s most important petrochemical, and steam cracking is by far the dominant method of production. In recent years, several economic trends have arisen that have motivated producers to examine alternative means for the cracking of hydrocarbons. Propylene demand is growing faster than ethylene demand, a trend that is expected to continue for the foreseeable future. Hydraulic fracturing in the United States has led to an oversupply of liquefied petroleum gas (LPG) which, in turn, has led to low ethane prices and a shift in olefin feedstock from naphtha to ethane. This shift to ethane has led to a relative reduction in the production of propylene. Conventional steam cracking of naphtha is limited by the kinetic behavior of the pyrolysis reactions to a propylene-to-ethylene ratio of 0.6–0.7. These trends have led producers to search for alternative ways to produce propylene. Several of these— propane dehydrogenation and metathesis, for example—have seen large numbers of newly constructed plants in recent years. Another avenue producers have examined is fluid catalytic cracking (FCC). FCC is the world’s second largest source of propylene. This propylene is essentially a byproduct of refinery gasoline production. However, in recent years, an effort has been made to increase ethylene and propylene yields to the point that these light olefins become the primary products. -
Experimental Investigation on the Mass Diffusion Behaviors of Calcium Oxide and Carbon in the Solid-State Synthesis of Calcium Carbide by Microwave Heating
molecules Article Experimental Investigation on the Mass Diffusion Behaviors of Calcium Oxide and Carbon in the Solid-State Synthesis of Calcium Carbide by Microwave Heating Miao Li 1,2 , Siyuan Chen 3, Huan Dai 1, Hong Zhao 1,* and Biao Jiang 1,3,* 1 Green Chemical Engineering Research Center, Shanghai Advanced Research Institute, Chinese Academy of Sciences, Shanghai 201210, China; [email protected] (M.L.); [email protected] (H.D.) 2 Green Chemical Engineering Research Center, Shanghai Advanced Research Institute, University of Chinese Academy of Sciences, Beijing 100049, China 3 Shanghai Green Chemical Engineering Research Center, Shanghai Institute of Organic Chemistry, Chinese Academy of Sciences, Shanghai 200032, China; [email protected] * Correspondence: [email protected] (H.Z.); [email protected] (B.J.) Abstract: Microwave (MW) heating was proven to efficiently solid-synthesize calcium carbide at 1750 ◦C, which was about 400 ◦C lower than electric heating. This study focused on the investigation of the diffusion behaviors of graphite and calcium oxide during the solid-state synthesis of calcium carbide by microwave heating and compared them with these heated by the conventional method. The phase compositions and morphologies of CaO and C pellets before and after heating were carefully characterized by inductively coupled plasma spectrograph (ICP), thermo gravimetric (TG) Citation: Li, M.; Chen, S.; Dai, H.; analyses, X-ray diffraction (XRD), scanning electron microscopy (SEM), and X-ray photoelectron Zhao, H.; Jiang, B. Experimental spectroscopy (XPS). The experimental results showed that in both thermal fields, Ca and C inter- Investigation on the Mass Diffusion Behaviors of Calcium Oxide and diffused at a lower temperature, but at a higher temperature, the formed calcium carbide crystals Carbon in the Solid-State Synthesis of would have a negative effect on Ca diffusion to carbon. -
Case Study Board Voting Copy February 2013
Carbide Industries Case Study Board Voting Copy February 2013 Case Study U.S. Chemical Safety and Hazard Investigation Board Carbide Industries, LLC, Louisville, KY Electric Arc Furnace Explosion March 21, 2011 2 Killed, 2 Injured No. 2011-05-I-KY KEY ISSUES • Facility Siting • Normalization of Deviance • Consensus Standards INSIDE • Process Discussion • Incident Description • Emergency Response • Analysis • Key Findings • Recommendations On March 21, 2011, during calcium carbide production at the Carbide Industries plant in Louisville, KY, an electric arc furnace exploded, ejecting solid and powdered debris, flammable gases, and molten calcium carbide at temperatures near 3800°F (2100°C). Two workers died and two others were injured. CSB • Carbide Industries Case Study 1 Carbide Industries Case Study Board Voting Copy February 2013 TABLE OF CONTENTS 1.0 Introduction 2 2.0 Process Discussion 3 3.0 Emergency Planning and Response 6 4.0 Incident Description 7 5.0 Analysis 8 6.0 Key Findings 13 7.0 Recommendations 14 8.0 References 15 9.0 Appendix A: Simplified Diagram of Calcium Carbide process 16 FIGURE 1 1.0 INTRODUCTION Satellite view of the Carbide Industries Louisville facility, Two workers were killed and two were injured at the Carbide Industries, LLC facility in with furnace building circled Louisville, KY, on Monday, March 21, 2011, when an electric arc furnace (EAF) overpres- sured and emitted powdered debris, hot gases, and molten calcium carbide. The hot gases and debris blown from the furnace broke through the double-pane reinforced glass window of the control room, severely burning the two workers inside; they died within 24 hours from burn injuries. -
Cracking (Chemistry)
Cracking (chemistry) In petrochemistry, petroleum geology and organic chemistry, cracking is the process whereby complex organic molecules such as kerogens or long-chain hydrocarbons are broken down into simpler molecules such as light hydrocarbons, by the breaking of carbon-carbon bonds in the precursors. The rate of cracking and the end products are strongly dependent on the temperature and presence of catalysts. Cracking is the breakdown of a large alkane into smaller, more useful alkenes. Simply put, hydrocarbon cracking is the process of breaking a long chain of hydrocarbons into short ones. This process requires high temperatures.[1] More loosely, outside the field of petroleum chemistry, the term "cracking" is used to describe any type of splitting of molecules under the influence of heat, catalysts and solvents, such as in processes of destructive distillation or pyrolysis. Fluid catalytic cracking produces a high yield of petrol and LPG, while hydrocracking is a major source of jet fuel, Diesel fuel, naphtha, and again yields LPG. Contents History and patents Cracking methodologies Thermal cracking Steam cracking Fluid Catalytic cracking Hydrocracking Fundamentals See also Refinery using the Shukhov cracking References process, Baku, Soviet Union, 1934. External links History and patents Among several variants of thermal cracking methods (variously known as the "Shukhov cracking process", "Burton cracking process", "Burton-Humphreys cracking process", and "Dubbs cracking process") Vladimir Shukhov, a Russian engineer, invented and patented the first in 1891 (Russian Empire, patent no. 12926, November 7, 1891).[2] One installation was used to a limited extent in Russia, but development was not followed up. In the first decade of the 20th century the American engineers William Merriam Burton and Robert E. -
Catalytic Dehydrogenation of Ethane: a Mini Review of Recent Advances and Perspective of Chemical Looping Technology
catalysts Review Catalytic Dehydrogenation of Ethane: A Mini Review of Recent Advances and Perspective of Chemical Looping Technology Danis Fairuzov, Ilias Gerzeliev, Anton Maximov and Evgeny Naranov * Topchiev Institute of Petrochemical Synthesis, Russian Academy of Sciences, Leninskiy Prospect, 29, 119991 Moscow, Russia; [email protected] (D.F.); [email protected] (I.G.); [email protected] (A.M.) * Correspondence: [email protected] Abstract: Dehydrogenation processes play an important role in the petrochemical industry. High selectivity towards olefins is usually hindered by numerous side reactions in a conventional crack- ing/pyrolysis technology. Herein, we show recent studies devoted to selective ethylene production via oxidative and non-oxidative reactions. This review summarizes the progress that has been achieved with ethane conversion in terms of the process effectivity. Briefly, steam cracking, catalytic dehydrogenation, oxidative dehydrogenation (with CO2/O2), membrane technology, and chemical looping are reviewed. Keywords: ethylene; ethane; dehydrogenation; cracking; membrane technology; chemical looping 1. Introduction Citation: Fairuzov, D.; Gerzeliev, I.; Ethylene is one of the most critical intermediates in the petrochemical industry and Maximov, A.; Naranov, E. Catalytic the global demand for this chemical is shown in Figure1; it is currently produced through Dehydrogenation of Ethane: A Mini the steam cracking of light hydrocarbon derivatives, mainly ethane and naphtha [1–3]. Review of Recent Advances and Ethylene complexes operate in 57 countries of the world. There are 215 ethylene producing Perspective of Chemical Looping facilities operating in the world. The operators of these complexes are about 100 companies, Technology. Catalysts 2021, 11, 833. and the largest are ExxonMobil, SABIC, DowDuPont [4–6]. -
Steam Cracking: Chemical Engineering
Steam Cracking: Kinetics and Feed Characterisation João Pedro Vilhena de Freitas Moreira Thesis to obtain the Master of Science Degree in Chemical Engineering Supervisors: Professor Doctor Henrique Aníbal Santos de Matos Doctor Štepánˇ Špatenka Examination Committee Chairperson: Professor Doctor Carlos Manuel Faria de Barros Henriques Supervisor: Professor Doctor Henrique Aníbal Santos de Matos Member of the Committee: Specialist Engineer André Alexandre Bravo Ferreira Vilelas November 2015 ii The roots of education are bitter, but the fruit is sweet. – Aristotle All I am I owe to my mother. – George Washington iii iv Acknowledgments To begin with, my deepest thanks to Professor Carla Pinheiro, Professor Henrique Matos and Pro- fessor Costas Pantelides for allowing me to take this internship at Process Systems Enterprise Ltd., London, a seven-month truly worthy experience for both my professional and personal life which I will certainly never forget. I would also like to thank my PSE and IST supervisors, who help me to go through this final journey as a Chemical Engineering student. To Stˇ epˇ an´ and Sreekumar from PSE, thank you so much for your patience, for helping and encouraging me to always keep a positive attitude, even when harder problems arose. To Prof. Henrique who always showed availability to answer my questions and to meet in person whenever possible. Gostaria tambem´ de agradecer aos meus colegas de casa e de curso Andre,´ Frederico, Joana e Miguel, com quem partilhei casa. Foi uma experienciaˆ inesquec´ıvel que atravessamos´ juntos e cer- tamente que a vossa presenc¸a diaria´ apos´ cada dia de trabalho ajudou imenso a aliviar as saudades de casa. -
Olefins from Biomass Intermediates: a Review
catalysts Review Review OlefinsOlefins fromfrom BiomassBiomass Intermediates:Intermediates: AA ReviewReview 1 1,2, VasilikiVasiliki Zacharopoulou Zacharopoulou1 andand AngelikiAngeliki A.A. LemonidouLemonidou 1,2,** 1 Department of Chemical Engineering, Aristotle University of Thessaloniki, University Campus, 1 Department of Chemical Engineering, Aristotle University of Thessaloniki, University Campus, Thessaloniki 54124, Greece; [email protected] 54124 Thessaloniki, Greece; [email protected] 2 Chemical Process Engineering Research Institute (CERTH/CPERI), P.O. Box 60361 Thermi, 2 Chemical Process Engineering Research Institute (CERTH/CPERI), P.O. Box 60361 Thermi, Thessaloniki 57001, Greece 57001 Thessaloniki, Greece * Correspondence: [email protected]; Tel.: +30‐2310‐996‐273 * Correspondence: [email protected]; Tel.: +30-2310-996-273 Received: 16 November 2017; Accepted: 19 December 2017; Published: Received: 16 November 2017; Accepted: 19 December 2017; Published: 23 December 2017 Abstract:Abstract: Over the last decade, increasing demand for olefinsolefins and theirtheir valuablevaluable productsproducts hashas promptedprompted researchresearch onon novelnovel processesprocesses andand technologiestechnologies forfor theirtheir selectiveselective production.production. As olefinsolefins are predominatelypredominately dependent on fossil resources, their production is limited by thethe finitefinite reservesreserves and the associated economic and environmental concerns.concerns. The need for alternative routes for -
Hydrocarbons Thermal Cracking Selectivity Depending on Their Structure and Cracking Parameters
Master in Chemical Engineering Hydrocarbons Thermal Cracking Selectivity Depending on Their Structure and Cracking Parameters Thesis of the Master’s Degree Development Project in Foreign Environment Cláudia Sofia Martins Angeira Erasmus coordinator: Eng. Miguel Madeira Examiner in FEUP: Eng. Fernando Martins Supervisor in ICT: Doc. Ing Petr Zámostný July 2008 Acknowledgements I would like to thank Doc. Ing. Petr Zámostný for the opportunity to hold a master's thesis in this project, the orientation, the support given during the laboratory work and suggestions for improvement through the work. i Hydrocarbons Thermal Cracking Selectivity Depending on Their Structure and Cracking Parameters Abstract This research deals with the study of hydrocarbon thermal cracking with the aim of producing ethylene, one of the most important raw materials in Chemical Industry. The main objective was the study of cracking reactions of hydrocarbons by means of measuring the selectivity of hydrocarbons primary cracking and evaluating the relationship between the structure and the behavior. This project constitutes one part of a bigger project involving the study of more than 30 hydrocarbons with broad structure variability. The work made in this particular project was focused on the study of the double bond position effect in linear unsaturated hydrocarbons. Laboratory experiments were carried out in the Laboratory of Gas and Pyrolysis Chromatography at the Department of Organic Technology, Institute of Chemical Technology, Prague, using for all experiments the same apparatus, Pyrolysis Gas Chromatograph, to increase the reliability and feasibility of results obtained. Linear octenes with different double bond position in hydrocarbon chain were used as model compounds. In order to achieve these goals, the primary cracking reactions were studied by the method of primary selectivities. -
Carbide Lamp
Carbide Lamp Equipment: washing bottle with dropping funnel rubber hose glass tube with tapered end matches or pocket lighter wooden splint test tube Chemicals: calcium carbide (ideal grain size: 20 – 40 mm) deionized water Safety: calcium carbide (CaC2): H260 P223, P231 + P232, P370 + P378, P422 ethyne (acetylene) (C2H2): H220 P210 calcium hydroxide (Ca(OH)2): H318 P280, P305 + P351 + P338, P313 Ethyne is extemely flammable and forms explosive mixtures with air (“detonating gas”). Because the gas is poisonous particularly with regard to contaminants it is necessary to work in a fume hood. It is also required to wear safety glasses and protective gloves. Procedure: The dropping funnel is filled with water and some lumps of calcium carbide are placed in the washing bottle. Water is dripped (cautiously!) onto the calcium carbide until a vigorous generation of gas begins. Then the cock of the dropping funnel is closed and the escaping gas is collected in the test tube. The existence of an explosive mixture can be tested by ignition with a burning splint. When the explosion danger is overcome, i.e. most of the air in the washing bottle is displaced by ethyne, the gas can be ignited directly at the tapered end of the glass tube by the splint (eventually, it is necessary to drip again some water onto the carbide). For avoiding any explosion danger it is recommended to fill the washing bottle with nitrogen before starting the experiment. Observation: The produced gaseous ethyne burns with a bright and sooty flame. Additionally, an unpleasant garlic-like odor can be noticed. -
Naphtha Catalytic Cracking for Propylene Production by FCCU
Naphtha Catalytic Cracking for Propylene Production by FCCU Christopher Dean - HIGH Olefins Technology Services LLC Coking and CatCracking Conference New Delhi, India – October 2013 Purpose (Objective) • To present and discuss producing propylene (C3=) by catalytic cracking paraffinic naphtha utilizing Fluid Catalytic Cracking processes 2 Contents- Covering 3 Points • Why Propylene from FCCU’s ? • Naphtha Feedstocks – Supply Balances • Naphtha Catalytic Cracking Processes • FCC Catalytic Processes • Traditional Steam Cracking (Comparison) 3 TYPICAL FCC Paraffinic Naphtha 4 Benefits • MOTOR GASOLINE • PETROCHEMICAL FEEDSTOCKS • Propylene (C3=) TODAY & FUTURE PLANNING • Minimizing to no gasoline production from FCC • Additional Focus • Light Olefins (Ethylene & Butylenes) • Aromatics 5 Why Propylene from FCCU’s ? • Europe, North America (US) refineries are facing profitability challenges • Gasoline demand declining both areas • Middle Distillates (Diesel) markets increasing both areas • European surplus gasoline export markets are declining • US lighter shale crudes, “tight oil” use is increasing that produce more naphtha and less diesel • Asia market is for distillates and petrochemical feedstocks • Large Middle East, Asia, India and South America are building large integrated Refinery/ Petrochemical 7 Complexes Petrochemicals Opportunities Produced by Steam Cracking Main Building Blocks Ethane & Liquid Feeds Naphtha Reformers • Olefins - Two Main Blocks • Ethylene • Propylene Secondary Source Produced by FCC’s • Aromatics • Benzene • -
Effects of Secondary Reaction of Primary Volatiles on Oil/Gas Yield and Quality from Oil Shale Pyrolysis
ISSN: 2638-1974 International Journal of Petrochemistry and Research Research Article Open Access Effects of Secondary reaction of Primary Volatiles on Oil/gas Yield and Quality from Oil Shale Pyrolysis Yuming Zhang1*, Rongxuan Linghu1, Lei Huang1, Liang Zhang1, Guogang Sun1 and Shu Zhang2* 1State Key Laboratory of Heavy Oil Processing, China University of Petroleum-Beijing, Beijing 102249, P.R.China 2College of Materials Science and Engineering, Nanjing Forestry University, Nanjing 210037, Jiangsu, P.R. China Article Info Abstract *Corresponding authors: The reaction behaviors of primary volatiles from oil shale pyrolysis were investigated Yuming Zhang using a two-stage reactor under different in-situ thermal reaction conditions. The secondary State Key Laboratory of Heavy Oil Processing reaction parameters, such as conversion temperature, reaction atmosphere and residence China University of Petroleum-Beijing time, were studied for their effects on the pyrolysis oil/gas yield and quality. The results Beijing 102249, P.R.China showed that the reaction temperature had a profound influence on the oil and gas yield, Tel: +86-15001296129 as indicated by the fact that the pyrolyzed shale oil and gas yield reduced by 15% (mass) E-mail: [email protected] and 20% (mass) respectively, with the temperature of 2nd stage reactor increasing from Shu Zhang ° ° College of Materials Science and 600 C to 650 C. Comparing with a nitrogen atmosphere, the liquid oil yield could enhance Engineering by 5% when steam was added as the reaction atmosphere in the second stage, and the Nanjing Forestry University corresponding oil was mainly concentrated in the gasoline and diesel distillations, that is, Nanjing 210037 boiling point <350°C. -
Naphtha Steam Cracking (NSC) Unit Optimization the Use of Robust On-Line Analyzer Technology for the Real-Time Optimization of Steam-Cracking Furnace Operation
— ABB MEASUREMENT & ANALYTICS | WHITE PAPER Naphtha Steam Cracking (NSC) unit optimization The use of robust on-line analyzer technology for the real-time optimization of steam-cracking furnace operation This white paper illustrates how the fast response times and excellent repeatability of on-line FT-NIR and other analyzers can be used to provide complete real-time data for the optimization of naphtha steam-cracking furnaces. Measurement made easy — First, we need to look at the background: why real-time also generate added-value co-products such as Refinery optimization of the steam-cracking furnace is so propylene, butenes (for butadiene production) necessary and what analytical tools exist to help. and a high aromatics content pygas product. This allows for operation of the steam-cracker in campaign Ethylene production runs at around 175 M tons mode, the better to tune product spectrum per year, the vast majority of which is produced to market opportunity. by steam-cracking light hydrocarbons – ethane where it is readily and cheaply available, liquid feeds Dr. Michael B. Simpson such as naphtha or, less commonly, gas oil where Industry Manager, Refining and Petrochemicals it is more advantageous. The use of naphtha as ABB Measurement & Analytics a feedstock has significant additional advantages where the end-customer market is dynamic in terms of demand and pricing, since naphtha feedstocks 2 NSC UNIT OPTIMIZATION | White Paper CH (off-gas) Acid gas 4 Quench/ fractionate Compression XXXX H S/CO 2 2 Methanator HC feed H Dryers 2 Demethanizer