Decarbonisation Options for Large Volume Organic Chemicals Production, Sabic Geleen
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Analysis of Trace Hydrocarbon Impurities in 1,3-Butadiene Using Optimized Rt®-Alumina BOND/MAPD PLOT Columns by Rick Morehead, Jan Pijpelink, Jaap De Zeeuw, Tom Vezza
Petroleum & Petrochemical Applications Analysis of Trace Hydrocarbon Impurities in 1,3-Butadiene Using Optimized Rt®-Alumina BOND/MAPD PLOT Columns By Rick Morehead, Jan Pijpelink, Jaap de Zeeuw, Tom Vezza Abstract Identifying and quantifying trace impurities in 1,3-butadiene is critical in producing high quality synthetic rubber products. Stan- dard analytical methods employ alumina PLOT columns which yield good resolution for low molecular weight hydrocarbons, but suffer from irreproducibility and poor sensitivity for polar hydrocarbons. In this study, Rt®-Alumina BOND/MAPD PLOT columns were used to separate both common light polar contaminants, including methyl acetylene and propadiene, as well as 4-vinylcy- clohexene, which is a high molecular weight impurity that normally requires a second test on an alternative column. By using an extended temperature program that employs the full thermal range of the column, 4-vinylcyclohexene, as well as all of the typical low molecular weight impurities in 1,3-butadiene, can be analyzed in a single test. Introduction 1,3-butadiene is typically isolated from products of the naphtha steam cracking process. Prior to purification, 1,3-butadiene can be contaminated with significant amounts of isobutene as well as other C4 isomers. In addition to removing these C4 isomeric contaminants during purification, it is also important that 1,3-butadiene be free of propadiene and methyl acetylene, which can interfere with catalytic polymerization. Alumina PLOT columns are the most commonly used GC column for this application, but the determination of polar hydrocarbon impurities at trace levels can be quite challenging and is highly dependent on the deactiva- tion of the alumina surface. -
Hoofdstuk 2 VOORGESCHIEDENIS
Hoofdstuk 2 VOORGESCHIEDENIS Vanaf hoofdstuk drie komen vele aspecten van het leven in Geleen-Zuid aan bod. Dit hoofdstuk gaat over ”alles wat er al was”. We beginnen met een samenvatting over de zware industrie, die voor de ontwikkeling van heel Geleen van groot belang was en is. Dit stuk is geschreven door Herman de Rooij, voormalig medewerker van DSM-Research. Daarna volgen stukken over bewoning aan de zuidzijde van Geleen voorafgaande aan de realisatie van Plan-Zuid. Met heel lang geleden sporen van Bandkeramiek en van recenter datum o.a. de beschrijving van het oude gehucht Spaans Neerbeek. Dit hoofdstuk wordt afgesloten met een vogelvlucht over de Christus Koningparochie, de jongste parochie van Geleen voordat Geleen- Zuid ontwikkeld werd. VAN STAATSMIJN MAURITS TOT CHEMELOT Voorwoord In 1915 besloot de Nederlandse regering om in Geleen-Lutterade een nieuwe mijn aan te leggen, die de naam Maurits kreeg. Geleen telde toen 3700 inwoners. De voornaamste bron van inkomsten was de landbouw. Een aardig beeld van die tijd, aan de vooravond van de mijnbouw, geeft het boek en de latere TV-serie ”Uit het dagboek van een herdershond”. Honderd jaar later wonen er tien maal zoveel mensen en is Geleen opgegaan in de gemeente Sittard-Geleen. De staatsmijnen heten nu DSM, de mijnbouw is verleden tijd, de fabrieken voor bulkchemie zoals kunstmest (SBB), naftakrakers, polyetheen en de polypropeen-fabrieken zijn verkocht en er is overgebleven een modern inter- nationaal opererende chemische onderneming, die als werkgebieden heeft: hoog- waardige kunststoffen, voeding en farma. De geschiedenis van Geleen is onlosmakelijk verbonden met de komst en groei van de staatsmijnen in Limburg, de latere DSM. -
Bereikbaarheid Zuyderland
versie maart 2021 Zuyderland Medisch Centrum 1 Sittard-Geleen Dr. H. van der Hoffplein 1, 6162 BG Sittard-Geleen T. 088 459 7777 2 Heerlen Henri Dunantstraat 5, 6419 PC Heerlen T. 088 459 7777 3 Kerkrade Wijngracht 45, 6461 AL Kerkrade T. 088 459 7777 Roermond 4 Brunssum Prins Hendriklaan 376, 6443 AE Brunssum T. 088 459 7777 5 Buitenpoli de Egthe De Egthe 1, 6101 EX Echt T. 0475 41 7887 Revalidatie 6 Revalidatie Dr. H. van der Hoffplein 1, 6162 BG Sittard - Geleen T. 088 459 7777 5 19 18 Echt Geestelijke Gezondheidszorg 7 Sittard-Geleen Dr. H. van der Hoffplein 1, 6162 BG Sittard - Geleen T. 088 459 9393 Susteren 8 Heerlen Henri Dunantstraat 5, 6419 PC Heerlen T. 088 459 7777 9 Kerkrade Wijngracht 45, 6461 AL Kerkrade T. 088 459 7777 Born 39 28 10 Brunssum Prins Hendriklaan 376, 6443 AE Brunssum T. 088 459 7777 20 11 Hostel & Inloop Stationsstraat 18-20, 6131 AZ Sittard T. 088 459 4040 35 12 DAC het Karwei Kastelenweg 1-3, 6136 BK Sittard T. 046 451 8914 13 13 Het Arbeidscentrum Millenerweg 8, 6131 KW Sittard T. 046 458 2789 21 15 22 14 16 14 Kinderpsych. dagbeh. Valkstraat 2a, 6135 GC Sittard (Het Drakennest & Het Vossenhol) T. 046 451 8914 12 15 Deeltijdbeh. Ouderen Gelderhof 2, 6136 CC Sittard T. 046 458 3011 Sittard 38 24 16 Kind en Adolecent Geerweg 5, 6135 KB Sittard T. 088 459 0330 32 11 31 17 23 6 zuyderland Geleen 7 1 Zuyderland Zorgcentra 30 27 34 Stein 37 17 Zorgcentra Kantoor Parklaan 10, 6131 KG Sittard T. -
Next Generation PLOT Alumina Technology for Accurate Measurement of Trace Polar Hydrocarbons in Hydrocarbon Streams
Next generation PLOT alumina technology for accurate measurement of trace polar hydrocarbons in hydrocarbon streams Jaap de Zeeuw, Tom Vezza, Bill Bromps, Rick Morehead and Gary Stidsen Restek Corporation, Bellefonte, USA 1 Next generation PLOT alumina technology for accurate measurement of trace polar hydrocarbons in hydrocarbon streams Jaap de Zeeuw, Tom Vezza, Bill Bromps, Rick More head and Gary Stidsen Restek Corporation Summary In light hydrocarbon analysis, the separation and detection of traces of polar hydrocarbons like acetylene, propadiene and methyl acetylene is very important. Using commercial alumina columns with KCl or Na2SO4 deactivation, often results in low response of polar hydrocarbons. Additionally, challenges are observed in response-in time stability. Solutions have been proposed to maximize response for components like methyl acetylene and propadiene, using alumina columns that were specially deactivated. Operating such columns showed still several challenges: Due to different deactivations, the retention and loadability of such alumina columns has been drastically reduced. A new Alumina deactivation technology was developed that combined the high response for polar hydrocarbon with maintaining the loadability. This allows the high response for components like methyl acetylene, acetylene and propadiene, also to be used for impurity analysis as well as TCD type applications. Such columns also showed excellent stability of response in time, which was superior then existing solutions. Additionally, it was observed that such alumina columns could be used up to 250 C, extending the Tmax by 50C. This allows higher hydrocarbon elution, faster stabilization and also widens application scope of any GC where multiple columns are used. In this poster the data is presented showing the improvements made in this important application field. -
Wide Range Linear Alpha Olefin Processes
IHS Chemical Process Economics Program Consolidated Report CR001 Wide Range Linear Alpha Olefin Processes By Marianna Asaro July 2014 ihs.com/chemical IHS Chemical Process Economics Program Consolidated Report | CR001 IHS Chemical agrees to assign professionally qualified personnel to the preparation of the Process Economics Program’s reports and will perform the work in conformance with generally accepted professional standards. No other warranties expressed or implied are made. Because the reports are of an advisory nature, neither IHS Chemical nor its employees will assume any liability for the special or consequential damages arising from the Client’s use of the results contained in the reports. The Client agrees to indemnify, defend, and hold IHS Chemical, its officers, and employees harmless from any liability to any third party resulting directly or indirectly from the Client’s use of the reports or other deliverables produced by IHS Chemical pursuant to this agreement. For detailed marketing data and information, the reader is referred to one of the IHS Chemical programs specializing in marketing research. The IHS CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced throughout the world. In addition the IHS DIRECTORY OF CHEMICAL PRODUCERS services provide detailed lists of chemical producers by company, product, and plant for the United States, Europe, East Asia, China, India, South & Central America, the Middle East & Africa, Canada, and Mexico. July 2014 ii © 2014 IHS IHS Chemical Process Economics Program Consolidated Report | CR001 PEP Report CR001 Wide Range Linear Alpha Olefin Processes By Marianna Asaro July 2014 Abstract This report consolidates and updates the Process Economics Program’s technical and economic analyses of wide-range linear alpha olefins (LAO) manufacturing technologies since PEP first reported on the subject in the 1960s. -
Isobutylene Polymer Having Unsaturated Group and Preparation
Europaisches Patentamt European Patent Office Office europeen des brevets (11) EP 0 452 875 B2 (12) NEW EUROPEAN PATENT SPECIFICATION (45) Date of publication and mention (51) |nt CI.6: C08F 10/10, C08F 2/42 of the opposition decision: 18.08.1999 Bulletin 1999/33 (45) Mention of the grant of the patent: 09.08.1995 Bulletin 1995/32 (21) Application number: 91106042.4 (22) Date of filing: 16.04.1991 (54) Isobutylene polymer having unsaturated group and preparation thereof Isobutylenpolymer mit ungesattigter Gruppe und seine Herstellung Polymere de I'isobutylene ayant un groupe insature et sa preparation (84) Designated Contracting States: (74) Representative: BE CH DE ES FR GB IT LI NL SE Hansen, Bernd, Dr. Dipl.-Chem. et al Hoffmann Eitle, (30) Priority: 16.04.1990 JP 10102990 Patent- und Rechtsanwalte, 29.11.1990 JP 33636490 Postfach 81 04 20 81904 Miinchen (DE) (43) Date of publication of application: 23.10.1991 Bulletin 1991/43 (56) References cited: EP-A- 0 265 053 EP-B- 0 322 241 (73) Proprietor: Kanegafuchi Chemical Industry Co., CA-A- 467 049 GB-A- 1 059 580 Ltd. US-A- 4 31 6 973 US-A- 4 327 201 Kita-ku Osaka-shi Osaka-fu (JP) US- A- 4 524 1 88 US-A- 4 758 63 1 US-A- 4 929 683 (72) Inventors: • Noda, Koji Remarks: Kobe-shi, Hyogo-ken (JP) The file contains technical information submitted • Fujisawa, Hiroshi after the application was filed and not included in this Kobe-shi, Hyogo-ken (JP) specification • Yonezawa, Kazuya Kobe-shi, Hyogo-ken (JP) CM DO 10 Is- 00 CM IO ^- o a. -
Model Vulcanization Systems for Butyl Rubber and Halobutyl Rubber Manual
Exxon™ butyl and halobutyl rubber Model vulcanization systems for butyl rubber and halobutyl rubber manual Country name(s) 2 - Model vulcanization systems for butyl rubber and halobutyl rubber manual Model vulcanization systems for butyl rubber and halobutyl rubber manual - 3 Abstract The vulcanization of isobutylene-co-isoprene rubber (IIR), brominated isobutylene-co-isoprene rubber (BIIR), chlorinated isobutylene-co-isoprene rubber (CIIR), and brominated isobutylene-co-para-methylstyrene elastomer (BIMSM) differs from that of general-purpose rubbers (GPR). Butyl rubber has approximately 2% unsaturation in the backbone. Halobutyl rubber (BIIR and CIIR) incorporates the butyl backbone with either bromine or chlorine, which significantly increases the chemical reactivity of the isoprenyl units located in the butyl backbone. Similarly, in BIMSM the bromine atom is bonded to the para-methylstyrene (PMS) group, thus affording the completely saturated polymer backbone a site of chemical reactivity. Utilization of the unique attributes of butyl rubber and halobutyl rubbers with their minimal backbone unsaturation and of BIMSM elastomers with no backbone unsaturation is found in many areas of industry. These properties are excellent vapor impermeation, resistance to heat degradation, and improved chemical resistance as compared to general-purpose rubbers. However, this low amount of reactivity requires special consideration to vulcanize these isobutylene-based polymers. The type of vulcanization system selected is a function of the composite structure in which it is used, and the cured product performance requirements. Therefore, vulcanization systems vary and may include an accelerator package along with resins, zinc oxide, zinc oxide and sulfur, and quinoid systems. This review will discuss the types and selection of appropriate vulcanization systems for isobutylene-based elastomers. -
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 -
Developing Linear-Alpha-Olefins Technology – from Laboratory to a Commercial Plant A
Catalysis – Innovative Applications in Petrochemistry and Refining DGMK Conference October 4-6, 2011, Dresden, Germany Developing Linear-alpha-Olefins Technology – From Laboratory to a Commercial Plant A. Meiswinkel, A. Wöhl, W. Müller, H. Bölt Linde AG, Pullach, Germany Abstract Linear α-Olefins (LAOs) are used in several applications in chemical industry. Together with SABIC (Saudi Basic Industries Corporation) Linde jointly developed the α-SABLIN technology for a full range LAO plant as well as a 1-Hexene selective "On Purpose" technology (LAO OP) to cover the rapidly increasing demand for this specific comonomer. The α-SABLIN as well as the OP technology are both homogenously catalyzed systems. This is raising special challenges concerning process and reactor design compared to much more established heterogeneous systems in chemical industry. E.g., the reactor concept is a bubble-column which allows efficient mixing as well as cooling of the reaction mixture. The development of the process was based on laboratory experiments which – based on an initial conceptual design for a large scale technical process - were first transformed into a pilot device before the commercial plant was designed, engineered and successfully started up and declared as commercialized. Today the α-SABLIN technology is the only LAO technology with a commercial reference which is free for licensing. A lot of experience and knowledge from the α-SABLIN development and commercial operation was gained. Although newly developed OP technology is based on a different catalytic system, this experience is now utilized and transformed within the commercialization of this new technological development. Introduction Linear α-Olefins (LAO) are used in several applications in chemical industry. -
Directory Global Directory 74 Sabic 70 Annual Report 2017 Directory 71
SABIC 68 ANNUAL REPORT 2017 69 MANUFACTURING COMPANIES 70 DIRECTORY GLOBAL DIRECTORY 74 SABIC 70 ANNUAL REPORT 2017 DIRECTORY 71 Petrochemicals MANUFACTURING Agri-Nutrients Specialties COMPANIES Metals* COMPANY LOCATION PARTNERSHIP PRODUCTS COMPANY LOCATION PARTNERSHIP PRODUCTS Alba Bahrain SABIC Industrial Investments Aluminum (liquid metal, ingots, Ibn Zahr Al-Jubail, SABIC (80%), Ecofuel-Italy (10%), MTBE and polypropylene Aluminium Bahrain** Company (20.62%), Bahrain rolling slabs, and billet) Saudi European Saudi Arabia Arab Petroleum Investment Mumtalakat Holding Company Petrochemical Corporation APICORP (10%) (69.38%), others/public (10%) Company Al-Bayroni Al-Jubail, A 50/50 SABIC joint-venture Ammonia, urea, 2-ethyl hexanol, Kemya Al-Jubail, A 50/50 SABIC joint-venture Polyethylene (LDPE, LLDPE), Al-Jubail Fertilizer Saudi Arabia with Taiwan Fertilizer Company and DOP Al-Jubail Saudi Arabia with Exxon Chemical Arabia ethylene, carbon black (CB), Company Petrochemical polybutadiene rubber (PBR), Company styrene butadiene rubber Ar-Razi Al Jubail, A 50/50 joint venture Chemical-grade methanol (SBR), ethylene propylene diene Saudi Methanol Saudi Arabia with Japan Saudi Arabia monomer (EPDM), regular butyl Ccompany Methanol Company (RB) and halo butyl (HB) Cos-Mar Company Caville, A 50/50 joint venture Styrene Ma’aden Phosphate Riyadh, SABIC (30%) and Ma’aden (70%) DAP, MAP, NPS Louisiana, USA with Total Company Saudi Arabia GARMCO Bahrain SABIC (30.40%), Bahrain Aluminum sheets and can stocks Ma’aden Wa’ad Riyadh, SABIC (15%), Mosaic -
FID Vs PID: the Great Debate
5/5/2017 FID vs PID: The Great Debate 2017 Geotechnical, GeoEnvironmental, and Geophysical Technology Transfer April 11, 2017 Raleigh, NC Why is it Important? As consultants, we are expected to produce data that is Reliable Repeatable Representative Defensible We can only meet these criteria if we understand the instruments we use and their limitations 1 5/5/2017 PID=Photo Ionization Detector Non-destructive to the sample Responds to functional groups Can operate in non-oxygen atmosphere Does not respond to methane Affected by high humidity FID=Flame Ionization Detector Destructive to the sample Responds to carbon chain length Must have oxygen to operate Responds to methane Not affected by high humidity 2 5/5/2017 Combination FID/PID TVA 1000B Main Concepts Ionization Energy Minimum amount of energy required to remove an electron from an atom or molecule in a gaseous state Response Factors The response factor is a calculated number provided by the instrument manufacturer for each compound, which is used to calculate the actual concentration of said compound in relation to the calibration gas. 3 5/5/2017 Ionization Energy Basis for FID/PID operations and measurement Measurements are in electron volts (eV) Ionization in a PID Energy source for ionization with PID is an ultraviolet light Three UV lamp energies are used: 9.5 eV, 10.6 eV, and 11.7 eV The higher the lamp energy, the greater the number of chemicals that can be detected. Detection range of 0.1 to 10,000 ppm 4 5/5/2017 Ionization in a FID Energy source for ionization -
Supplement of Compilation and Evaluation of Gas Phase Diffusion Coefficients of Reactive Trace Gases in the Atmosphere
Supplement of Atmos. Chem. Phys., 15, 5585–5598, 2015 http://www.atmos-chem-phys.net/15/5585/2015/ doi:10.5194/acp-15-5585-2015-supplement © Author(s) 2015. CC Attribution 3.0 License. Supplement of Compilation and evaluation of gas phase diffusion coefficients of reactive trace gases in the atmosphere: Volume 2. Diffusivities of organic compounds, pressure-normalised mean free paths, and average Knudsen numbers for gas uptake calculations M. J. Tang et al. Correspondence to: M. J. Tang ([email protected]) and M. Kalberer ([email protected]) The copyright of individual parts of the supplement might differ from the CC-BY 3.0 licence. Table of Contents 1 Alkanes and cycloalkanes ............................................................................................ 1 1.1 CH 4 (methane), C 2H6 (ethane), and C 3H8 (propane) ............................................. 1 1.2 C 4H10 (butane, methyl propane) ............................................................................ 3 1.3 C 5H12 (n-pentane, methyl butane, dimethyl butane) ............................................. 5 1.4 C 6H14 (n-hexane, 2,3-dimethyl butane) ................................................................ 7 1.5 C 7H16 (n-heptane, 2,4-dimethyl pentane).............................................................. 9 1.6 C 8H18 (n-octane, 2,2,4-trimethyl pentane) .......................................................... 11 1.7 C 9H20 (n-nonane), C 10 H22 (n-decane, 2,3,3-trimethyl heptane) and C 12 H26 (n- dodecane) .................................................................................................................