Production of Gasolines and Monocyclic Aromatic Hydrocarbons: from Fossil Raw Materials to Green Processes
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Petroleum Refinery Process Stream Additions
American Petroleum Institute Petroleum Refinery Process Stream Additions CasNo Substance Definition Caveat 129813-66-7 Alkanes, C10-13 68551-17-7 Alkanes, C10-13-iso- 93924-07-3 Alkanes, C10-14 68551-18-8 Alkanes, C10-14-iso- 329909-27-5 Alkanes, C10-15-iso-, cyclic and linear 73138-29-1 Alkanes, C10-18 289711-49-5 Alkanes, C10-24 289711-48-4 Alkanes, C10-24-branched 129813-67-8 Alkanes, C12-14 68551-19-9 Alkanes, C12-14-iso- 68551-20-2 Alkanes, C13-16-iso- 90622-46-1 Alkanes, C14-16 74664-93-0 Alkanes, C14-30 70024-92-9 Alkanes, C7-8-iso- 68551-15-5 Alkanes, C8-10-iso- 68551-16-6 Alkanes, C9-11-iso- 68990-23-8 Alkenes, C12-26 .alpha.-, sulfated 93762-80-2 Alkenes, C15-18 68603-35-0 Alkenes, C18-24 .alpha.-, bisulfited 72162-34-6 Alkenes, C18-24 .alpha.-, sulfurized 93924-10-8 Alkenes, C20-24 .alpha.- 93924-11-9 Alkenes, C24-28 .alpha.- 131459-42-2 Alkenes, C24-54-branched and linear .alpha.- 68409-73-4 Aromatic hydrocarbons, biphenyl-rich A complex combination of hydrocarbons produced by the Substance found at hydrodealkylation and distillation of toluene. It consists refineries, but also may be predominantly of aromatic hydrocarbons having a carbon number produced in separate C6 or greater, primarily biphenyl, and boiling in the range of petrochemical approximately 79.degree.C to 398.degree.C (175.degree.F to manufacturing facilities. 750.degree.F). 68989-41-3 Aromatic hydrocarbons, biphenyl-rich, The complex combination of hydrocarbons obtained from a Substance found at thermal hydrodealkylation residues thermal hydrodealkylation process. -
Including Toluene Derivatives
RSC Advances View Article Online PAPER View Journal | View Issue Catalytic C–H aerobic and oxidant-induced oxidation of alkylbenzenes (including toluene Cite this: RSC Adv., 2020, 10,23543 derivatives) over VO2+ immobilized on core–shell Fe3O4@SiO2 at room temperature in water† Pegah Mohammadpour and Elham Safaei * Direct C–H bond oxidation of organic materials, and producing the necessary oxygenated compounds under mild conditions, has attracted increasing interest. The selective oxidation of various alkylbenzenes 2+ was carried out by means of a new catalyst containing VO species supported on silica-coated Fe3O4 nanoparticles using t-butyl hydroperoxide as an oxidant at room temperature in H2O or solvent-free media. The chemical and structural characterization of the catalyst using several methods such as FTIR spectroscopy, XRD, FETEM, FESEM, SAED, EDX and XPS showed that VO2+ is covalently bonded to the silica surface. High selectivity and excellent conversion of various toluene derivatives, with less reactive Creative Commons Attribution 3.0 Unported Licence. Received 18th April 2020 aliphatic (sp3)C–H bonds, to related benzoic acids were quite noticeable. The aerobic oxygenation Accepted 15th May 2020 reaction of these alkylbenzenes was studied under the same conditions. All the results accompanied by DOI: 10.1039/d0ra03483e sustainability of the inexpensive and simple magnetically separable heterogeneous catalyst proved the rsc.li/rsc-advances important criteria for commercial applications. Introduction industrial communities. Among -
Refining/Petrochemical Integration-A New Paradigm Joseph C
Refining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate® Refining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing, GTC Technology US, LLC Introduction The global trend in motor fuel consumption favors diesel over gasoline. There is a simultaneous increase in demand for various petrochemicals such as propylene and aromatics. Technology provid- ers have been successful to utilize the Fluid Catalytic Cracking (FCC) unit as a method to produce propylene by high severity operation, but the potential for other petrochemicals from these units has been neglected. Cat cracked gasoline contains a high level of olefins, some sulfur, and appreciable aromatics. Until now, the aromatics were not wanted due to the olefin and sulfur impurities in this stream. New technology is being commercialized to separate the aromatics from FCC gasoline in order to use them directly for downstream applications. Additionally, the olefin fraction can be converted into aromatics through a simple fixed-bed reaction system. Thus all of the gasoline components are efficiently made into high-value petrochemicals. This combination of technology is much more efficient than methods that some operators use, which recycles FCC gasoline to the reforming unit. Aromatics is a fast growing market. CMAI (acquired by IHS in 2011) in 2005 forecast benzene demand to grow at 4.1% per year between 2000 and 2020, resulting in total demand growth of 24.3 million tons.1 Mixed xylenes capacity will approximately double by 2020 to meet the strong antici- pated demand growth, mainly driven by the strong demand for polyester. -
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. -
ECO-Ssls for Pahs
Ecological Soil Screening Levels for Polycyclic Aromatic Hydrocarbons (PAHs) Interim Final OSWER Directive 9285.7-78 U.S. Environmental Protection Agency Office of Solid Waste and Emergency Response 1200 Pennsylvania Avenue, N.W. Washington, DC 20460 June 2007 This page intentionally left blank TABLE OF CONTENTS 1.0 INTRODUCTION .......................................................1 2.0 SUMMARY OF ECO-SSLs FOR PAHs......................................1 3.0 ECO-SSL FOR TERRESTRIAL PLANTS....................................4 5.0 ECO-SSL FOR AVIAN WILDLIFE.........................................8 6.0 ECO-SSL FOR MAMMALIAN WILDLIFE..................................8 6.1 Mammalian TRV ...................................................8 6.2 Estimation of Dose and Calculation of the Eco-SSL ........................9 7.0 REFERENCES .........................................................16 7.1 General PAH References ............................................16 7.2 References Used for Derivation of Plant and Soil Invertebrate Eco-SSLs ......17 7.3 References Rejected for Use in Derivation of Plant and Soil Invertebrate Eco-SSLs ...............................................................18 7.4 References Used in Derivation of Wildlife TRVs .........................25 7.5 References Rejected for Use in Derivation of Wildlife TRV ................28 i LIST OF TABLES Table 2.1 PAH Eco-SSLs (mg/kg dry weight in soil) ..............................4 Table 3.1 Plant Toxicity Data - PAHs ..........................................5 Table 4.1 -
Reactions of Benzene Or Alkylbenzenes with Steam Over a Silica-Supported Nickel Catalyst*
54 Reactions of Benzene or Alkylbenzenes with Steam over a Silica-supported Nickel Catalyst* by .Masahiro Saito**, Yoshio Sohda** Michiaki Tokuno** and Yoshiro Morita** Summary: Benzene-steam and alkylbenzenes-steam reactions over a silica-supported nickel catalyst have been studied under atmospheric pressure in a temperature range of 370~430℃. In the reactionof benzene-steam,the methaneyield is lower and the carbon dioxideyield is higher than the estimatedvalue. The reactionis zero order with respectto benzeneand approxi- mately first order with respect to steam. In the reactionof alkylbenzenes-steam,ring breakdownand dealkylationoccur at the initial stage of reaction, and theformer occursmore easily than the latter at high conversionand at high temperature. The number and the position of the alkyl group on the benzene ring influencethe reaction rate and the selectivity. The reactionpath of dealkylationis proposed as follows: most effective catalyst for dealkylation with 1 Introduction steam, and they investigated reactivity and reac- The catalytic reaction of hydrocarbon with tion path on Ni/BeO at 450℃. steam is important for the production of hydrogen, In the present work, the reactions of benzene synthesis gas and town gas. The authors have or alkylbenzenes with steam were carried out previously reported the works on olefins-steam over a silica-supported nickel catalyst under and paraffins-steam reactions over a silica-sup- atmospheric pressure in a temperature range of ported nickel catalyst1)~3), and this study on 370~430℃, and the effects of reaction conditions, aromatics-steam reactions has been carried out rate of each reaction and the reaction path were as a consecutive one. -
Disproportionation and Transalkylation of Alkylbenzenes Over Zeolite Catalysts
Applied Catalysis A: General 181 (1999) 355±398 Disproportionation and transalkylation of alkylbenzenes over zeolite catalysts Tseng-Chang Tsaia, Shang-Bin Liub, Ikai Wangc,* aRe®ning and Manufacturing Research Center, Chinese Petroleum Corporation, Chiayi 600, Taiwan bInstitute of Atomic and Molecular Sciences, Academia Sinica, PO Box 23-166, Taipei 106, Taiwan cDepartment of Chemical Engineering, National Tsing-Hua University, Hsinchu 300, Taiwan Received 13 June 1998; received in revised form 3 October 1998; accepted 5 November 1998 Abstract Disproportionation and transalkylation are important processes for the interconversion of mono-, di-, and tri-alkylbenzenes. In this review, we discuss the recent advances in process technology with special focus on improvements of para-isomer selectivity and catalyst stability. Extensive patent search and discussion on technology development are presented. The key criteria for process development are identi®ed. The working principles of para-isomer selectivity improvements involve the reduction of diffusivity and the inactivation of external surface. In conjunction with the fundamental research, various practical modi®cation aspects particularly the pre-coking and the silica deposition techniques, are extensively reviewed. The impact of para-isomer selective technology on process economics and product recovery strategy is discussed. Furthermore, perspective trends in related research and development are provided. # 1999 Elsevier Science B.V. All rights reserved. Keywords: Disproportionation; Transalkylation; -
Trimethylbenzenes CAS Registry Numbers: 526-73-6 (1,2,3-TMB) 95-63-6 (1,2,4-TMB) 108-67-8 (1,3,5-TMB) 25551-13-7 (Mixed Isomers)
Development Support Document Final, September 4, 2015 Trimethylbenzenes CAS Registry Numbers: 526-73-6 (1,2,3-TMB) 95-63-6 (1,2,4-TMB) 108-67-8 (1,3,5-TMB) 25551-13-7 (Mixed Isomers) Prepared by Joseph T. Haney, Jr., M.S. Angela Curry, M.S. Toxicology Division Office of the Executive Director TEXAS COMMISSION ON ENVIRONMENTAL QUALITY Trimethylbenzenes Page i TABLE OF CONTENTS TABLE OF CONTENTS ............................................................................................................................................ I LIST OF TABLES ......................................................................................................................................................II ACRONYMS AND ABBREVIATIONS ................................................................................................................. III CHAPTER 1 SUMMARY TABLES .......................................................................................................................... 1 CHAPTER 2 MAJOR SOURCES AND USES ......................................................................................................... 4 CHAPTER 3 ACUTE EVALUATION ...................................................................................................................... 4 ACUTE 3.1 HEALTH-BASED ACUTE REV AND ESL ........................................................................................................ 4 3.1.1 Physical/Chemical Properties .................................................................................................................... -
BTX) / Hydrotreated Pygas (HPG)
Product Stewardship Summary Benzene, Toluene, Xylene Mixture (BTX) / Hydrotreated Pygas (HPG) The product stewardship summary is intended to give general information about the chemical or categories of chemicals addressed. It is not intended to provide an in-depth discussion of all health and safety information. Additional information on this chemical is available through the applicable Material Safety Data Sheet which must be consulted before using this chemical. The product stewardship summary does not supplant or replace required regulatory and/or legal communication documents. Chemical Identity: Benzene/Toluene/Xylene Mixture (BTX), also known as Hydrogenated Pyrolysis Gasoline (HPG), is a clear liquid with an aromatic odor. BTX/HPG is a co-product of ethylene production and is produced in closed systems that are monitored and controlled. HPG (BTX) is made by the double hydrogenation of raw pyrolysis gasoline (RPG), also known as debutanized aromatic concentrate (DAC). CAS Number: 68410-97-9 Synonyms:Pyrolysis Gasoline, High Benzene Naphtha, Aromatic Concentrate, Light Hydrotreated Distillate Product Uses: There are no consumer uses of BTX/HPG. BTX/HPG is used primarily as feedstock for benzene extraction. The remaining components are further separated into toluene and xylene. Benzene is primarily used for ethylbenzene to styrene and cumene to phenol production. The third largest use of benzene is in the production of cyclohexane, a nylon precursor. Toluene, the second largest aromatic in BTX/HPG, is used in refinery streams such as gasoline blending for its octane value. Xylenes may either be used in refinery streams for gasoline blending or further separated by isomers for chemical applications. Physical/Chemical Properties: BTX/HPG is classified by the U.S. -
Acrylonitrile
Common Name: ACRYLONITRILE CAS Number: 107-13-1 DOT Number: UN 1093 (Inhibited) RTK Substance number: 0024 DOT Hazard Class: 3 (Flammable Liquid) Date: May 1998 Revisions: December 2005 ------------------------------------------------------------------------- ------------------------------------------------------------------------- HAZARD SUMMARY * Acrylonitrile can affect you when breathed in and by training concerning chemical hazards and controls. The federal passing through your skin. OSHA Hazard Communication Standard 29 CFR 1910.1200, * Acrylonitrile is a CARCINOGEN--HANDLE WITH requires private employers to provide similar training and EXTREME CAUTION. information to their employees. * Acrylonitrile should be handled as a TERATOGEN-- WITH EXTREME CAUTION. * Exposure to hazardous substances should be routinely * Skin contact can cause severe irritation and blistering. evaluated. This may include collecting personal and area air * Exposure to Acrylonitrile can irritate the eyes, nose, and samples. You can obtain copies of sampling results from throat. your employer. You have a legal right to this information * Breathing Acrylonitrile can irritate the lungs causing under the OSHA Standard 29 CFR 1910.1020. coughing and/or shortness of breath. Higher exposures can * If you think you are experiencing any work-related health cause a build-up of fluid in the lungs (pulmonary edema), a problems, see a doctor trained to recognize occupational medical emergency, with severe shortness of breath. diseases. Take this Fact Sheet with you. * Exposure to Acrylonitrile can cause weakness, headache, * ODOR THRESHOLD = 1.6 ppm. dizziness, confusion, nausea, vomiting, and can lead to * The range of accepted odor threshold values is quite broad. death. Caution should be used in relying on odor alone as a * Repeated exposure can irritate the nose causing discharge, warning of potentially hazardous exposures. -
Studies of the Temporary Anion States of Unsaturated Hydrocarbons by Electron Transmission Spectroscopy
University of Nebraska - Lincoln DigitalCommons@University of Nebraska - Lincoln Paul Burrow Publications Research Papers in Physics and Astronomy 1978 Studies of the Temporary Anion States of Unsaturated Hydrocarbons by Electron Transmission Spectroscopy Kenneth D. Jordan Paul Burrow Follow this and additional works at: https://digitalcommons.unl.edu/physicsburrow Part of the Atomic, Molecular and Optical Physics Commons This Article is brought to you for free and open access by the Research Papers in Physics and Astronomy at DigitalCommons@University of Nebraska - Lincoln. It has been accepted for inclusion in Paul Burrow Publications by an authorized administrator of DigitalCommons@University of Nebraska - Lincoln. digitalcommons.unl.edu Studies of the Temporary Anion States of Unsaturated Hydrocarbons by Electron Transmission Spectroscopy Kenneth D. Jordan Mason Laboratory, Department of Engineering and Applied Science, Yale University, New Haven, Connecticut 06520 Paul D. Burrow Behlen Laboratory of Physics, University of Nebraska, Lincoln, Nebraska 68588 The concept of occupied and unoccupied orbitals has provided a useful means for visualizing many of the most important properties of mo- lecular systems. Yet, there is a curious imbalance in our experimen- tal knowledge of the energies of occupied and unoccupied orbitals. Whereas photoelectron spectroscopy has provided a wealth of data on positive ion states and has established that they can be associated, within the context of Koopmans’ theorem, with the occupied orbitals of the neutral molecule, the corresponding information for the neg- ative ion states, associated with the normally unoccupied orbitals, is sparse. In part this reflects the experimental difficulties connected with measuring the electron affinities of molecules which possess sta- ble anions. -
BENZENE Disclaimer
United States Office of Air Quality EPA-454/R-98-011 Environmental Protection Planning And Standards June 1998 Agency Research Triangle Park, NC 27711 AIR EPA LOCATING AND ESTIMATING AIR EMISSIONS FROM SOURCES OF BENZENE Disclaimer This report has been reviewed by the Office of Air Quality Planning and Standards, U.S. Environmental Protection Agency, and has been approved for publication. Mention of trade names and commercial products does not constitute endorsement or recommendation of use. EPA-454/R-98-011 ii TABLE OF CONTENTS Section Page LIST OF TABLES.....................................................x LIST OF FIGURES.................................................. xvi EXECUTIVE SUMMARY.............................................xx 1.0 PURPOSE OF DOCUMENT .......................................... 1-1 2.0 OVERVIEW OF DOCUMENT CONTENTS.............................. 2-1 3.0 BACKGROUND INFORMATION ...................................... 3-1 3.1 NATURE OF POLLUTANT..................................... 3-1 3.2 OVERVIEW OF PRODUCTION AND USE ......................... 3-4 3.3 OVERVIEW OF EMISSIONS.................................... 3-8 4.0 EMISSIONS FROM BENZENE PRODUCTION ........................... 4-1 4.1 CATALYTIC REFORMING/SEPARATION PROCESS................ 4-7 4.1.1 Process Description for Catalytic Reforming/Separation........... 4-7 4.1.2 Benzene Emissions from Catalytic Reforming/Separation .......... 4-9 4.2 TOLUENE DEALKYLATION AND TOLUENE DISPROPORTIONATION PROCESS ............................ 4-11 4.2.1 Toluene Dealkylation