Industrial Carbon and Graphite Materials. Группа авторов. Читать онлайн. Newlib. NEWLIB.NET

Автор: Группа авторов
Издательство: John Wiley & Sons Limited
Серия:
Жанр произведения: Техническая литература
Год издания: 0
isbn: 9783527674053
Скачать книгу
Process) to the CLP regulation Commission Regulation EU, No. 286, 2011 ‐ CONCAWE recommendations, August 2001; CLP according to the EU dangerrous substances directive ‐ API (American Petroleum Institut) – Report:”Petroleum Coke Category Analysis and Hazard Charakterization”.

      4 4 Sojka, M. (2011). Orinoco Oil Belt, PH 240, Stanford University.

      5 5 Dunbar, R.B. (2012). Strategy West Inc., Canada’Oil Sands, Internet.

      6 6 Chandelle, J.M. (2005). CEM Rev. 220: 1–22.

      7 7 Jacobs Consultancy Offices (2011). 10th Annual Petcoke Conference, San Diego, CA.

      8 8 Statistik der Kohlewirtschaft, Essen (1995).

      9 9 EIA (2013). U.S. Energy Information Administration, March 2013.

      10 10 Billege, I. (2009). 700 refineries supply oil products to the world. NAFTA 60 (7–8): 401–403.

      11 11 Predel, H. (1990). Delayed coking. Erdöl Kohle Erdgas Petrochem. 43: 145–146.

      12 12 Conoco Inc. (1984). Method of reducing coke yield. US 44,55,219 (H.R. Janssen, G.L. Poffenbarger).

      13 13 Conoco Inc. (1985). Process for improving product yields from delayed coking. US 45,18,487 (H.G. Graf, H.R. Janssen).

      14 14 Elliott, J.D. (2008). ImpaCT of feed properties and operating parameters on delayed coker petcoke quality. Presented at ERTC Conference

      15 15 Predel, H. (1992). Theoretical and practical methods for coke yield calculations and optimisation. In: Light Metals 1992, 601–609. San Diego, CA: TMS.

      16 16 Liebermann, N. (1985). Troubleshooting in Process Operations, 16–26. Metairie, LA: Pen Well Publishing Comp.

      17 17 Predel, H. (1992). New developments in delayed coker operations. Carbon Conference (22–26 June 1992). Essen.

      18 18 Stefani, A. (1996). Debottleneck delayed cokers for greater profitability. Hydrocarbon Process. 6: 99–103.

      19 19 Mobil Oil Corporation (1978). Conversion of solid wastes to fuel coke and gasoline. US 4,118,281 (T.‐Y. Yan).

      20 20 Elliott, J.D. and Klick, R. (1994). Trends in delayed coker design. Hydrocarbon Technol. Int. J. 71 (1) Summer): 17–23.

      21 21 Elliott, J.D. (1993). Latest coker designs increase liquid yields, reduce emissions. Oil Gas J. 91: 14–20.

      22 22 Elliott, J.D. (1992). Maximize distillate liquid products. Hydrocarbon Process. 71 (1): 79–84.

      23 23 NPRA (National Petroleum Refiners Association) (1994). Refiners exchange experiences on FCC problems, coking operations. Oil Gas J. 92: 110–115.

      24 24 Parrish, M.R., Hammond, D.G., and Citarella, V.A. (1996). Fluid coking: a continuous, flexible and reliable conversion process. Hydrocarbon Technol. Int. J. Spring: 25–31.

      25 25 Diff. autors (1996). Refining 1996, Hydrocarbon Process. 75 Special Edition, November 100.

      26 26 Predel, H. (1996). Steps for green coke calcination‐mathematic model and practical tests and experiences. In: Light Metals 1996, 499–507. Los Angeles, CA: TMS.

      27 27 Fischer, W.K., Collin, G., and Stadelhofer, J.W. (1990). Technischer Kohlenstoff—Herstellung und Anwendung. DGMK‐Haupttagung, Essen, September 1921, 423.

      28 28 Mochida, J., Fujimoto, K., and Oyama, T. (1997). Chemistry in the production and utilization of needle coke. In: Chemistry and Physics of Carbon, vol. 25 (ed. P.A. Thore), 111–212. New York, NY, Basel, Hongkong: Marcel Dekker.

      29 29 Predel, H. (2005). Erdöl Erdgas Kohle 121: 348–352, Petroleum Koks‐Entwicklung und Tendenzen H.Predel, OIL GAS European Magazine, 4 (2008) 2004–205,Commercial Incentive for the Production of High Quality Petroleum Coke Calcinate H.Predel, OIL GAS European Magazine, 2 (2013). 98–100, Important Steps for Production of High‐Quality Petroleum Coke Calcinate.

      30 30 Karlsruher Institut für Technology (2009). Presseinformation Nr.143, Dez. 2009.

      31 31 Roskill Information Services (2005). Petroleum Coke Market Research. Global Information, Inc.

      32 32 International Aluminium Institute (2005). Statistical Report, London.

      33 33 Edwards, L., Backhouse, N., Darmstadt, H., and Dion, M.‐J. (2012). Evolution of anode grade coke quality. In: Ligth Metals 2012, 35–39. Las Vegas, NV.

      34 34 Adams, R., Frohs, W., Jäger, H., and Roussel, K. (2007). Graphite and Needle Coke Development. Conoco Phillips, SGL Group. http://www.asc.omnibooks.

      35 35 Halim, H., Im, J., and Lee, C. (2013). Preparation of needle coke from petroleum by‐products. Carbon Lett. 14 (3): 152–161.

      36 36 SGL Group (2012). Investor Relations Presentation.

      37 37 Global and China Needle Coke, Industry Report 2012–2015, Research in China.

      38 38 Blumberg, H. (1997). Fibers for composites status quo and trends. Chem. Fibers Int. 47: 36–41.

      39 39 Jonville, C., Thomas, J.C., and Dreyer, C. (1995). The influence of coke source on anode performance. JOM 47: 23–24.

      40 40 Hume, S.M., Fischer, W.K., Perruchoud, R.C., and Welch, B. (1993). A model for petroleum coke reactivity. In: Light Metals 1993, 525–534. San Diego, CA: TMS.

      41 41 Keller, F. and Mannweiler, U. (1995). Anode Performance: The Link between Coke Properties and Aluminum Production Cost. PACE, Petroleum Coke Quarterly.

      42 42 Conoco Inc. Method for producing Premium Coke from residual coke. US Patent 4,235,703, 1980.

      43 43 Jieming, X., Guo, F., Miglan, G., and Yanging, Z. (2012). Preparation on high quality needle coke from FCC decant oil. In: International Conference on Solid State and Materials, Lecture Notes in Information Technology, vol. 22.

      44 44 Kalincheva, L., Zaporin, V., and Knatmullin, I. (1996). Influence of coker feed properties on quality of graphitized electrodes. Chem. Technol. Fuels Oils 32 (2): 80–81.

      45 45 Meier, M.W. (1996). Cracking Behavior of Anodes. Sierre: R+D Carbon Ltd.

      Further Reading

      1 Escallon, M. (2011). Petroleum and Petroleum/Coal Blends as Feedstocks, paperback‐book.

      2 Fahim, M.A., Alsahhaf, T.A., and Elkilani, A.S. (2010). Fundamentals of Petroleum Refining. Amsterdam: Elsevier.

      3 Hsu, C.S. and Robin, P.R. (2006). Practical Advances in Petroleum Processing. New York, NY: Springer.

      4 Qahtani, K.Y.A. and Elkamel, A. (2010). Planning and Integration of Refinery and Petrochemical Operations. Weinheim: Wiley‐VCH.

      5 Speight, J.G. (2000). Petroleum refinery processes. In: Kirk Othmer Encyclopedia of Chemical Technology, 5e. Hoboken, NJ: Wiley.

      Note

      1 * A previous version of this article has been published in Ullmann’s Encyclopedia of Industrial Chemistry.

       Tetsusei Fukuda

       C‐Chem Co. Ltd, Tokyo, Japan

      6.1.3.1. Introduction

      Pitch coke (hereinafter referred to as PC) is a blocky, granular, and powdery, black carbonaceous substance with maximum diameter of approximately 30 mm and with pores or cracks visible to naked eyes as manufactured by the carbonization at temperature equal to or higher than approximately 450 °C of coal‐tar pitch as a raw material withdrawn from the bottom of a distillation column in which coal tar described in Section 6.1.5.3.4 is distilled. PC contains nearly free of ash. This is a big difference from similar