New Trends in Olefin Production

Ismaël Amghizar, Laurien A. Vandewalle, Kevin M. Van Geem, Guy B. Marin

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Engineering ›› 2017, Vol. 3 ›› Issue (2) : 171-178. DOI: 10.1016/J.ENG.2017.02.006
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New Trends in Olefin Production

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Abstract

Most olefins (e.g., ethylene and propylene) will continue to be produced through steam cracking (SC) of hydrocarbons in the coming decade. In an uncertain commodity market, the chemical industry is investing very little in alternative technologies and feedstocks because of their current lack of economic viability, despite decreasing crude oil reserves and the recognition of global warming. In this perspective, some of the most promising alternatives are compared with the conventional SC process, and the major bottlenecks of each of the competing processes are highlighted. These technologies emerge especially from the abundance of cheap propane, ethane, and methane from shale gas and stranded gas. From an economic point of view, methane is an interesting starting material, if chemicals can be produced from it. The huge availability of crude oil and the expected substantial decline in the demand for fuels imply that the future for proven technologies such as Fischer-Tropsch synthesis (FTS) or methanol to gasoline is not bright. The abundance of cheap ethane and the large availability of crude oil, on the other hand, have caused the SC industry to shift to these two extremes, making room for the on-purpose production of light olefins, such as by the catalytic dehydrogenation of propane.

Keywords

Olefin production / Steam cracking / Methane conversion / Shale gas / CO2 emissions

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Ismaël Amghizar, Laurien A. Vandewalle, Kevin M. Van Geem, Guy B. Marin. New Trends in Olefin Production. Engineering, 2017, 3(2): 171‒178 https://doi.org/10.1016/J.ENG.2017.02.006

References

[1]
Zimmermann H, Walzl R. Ethylene. In: Ullmann's encyclopedia of industrial chemistry. Weinheim: Wiley-VCH Verlag GmbH & Co. KGaA; 2009.
[2]
BP plc. BP statistical review of world energy. BP technical report. London: BP plc; 2013 Jun.
[3]
United States Energy Information Administration. Annual energy outlook 2015 with projections to 2040. Washington, DC: United States Energy Information Administration; 2015.
[4]
Sattler JJ, Ruiz-Martinez J, Santillan-Jimenez E, Weckhuysen BM. Catalytic dehydrogenation of light alkanes on metals and metal oxides. Chem Rev 2014;114(20):10613–53.
CrossRef Google scholar
[5]
Bruijnincx PC, Weckhuysen BM. Shale gas revolution: An opportunity for the production of biobased chemicals? Angew Chem Int Ed Engl 2013;52(46):11980–7.
CrossRef Google scholar
[6]
Siirola JJ. The impact of shale gas in the chemical industry. AIChE J 2014;60(3):810–9.
CrossRef Google scholar
[7]
Yang CJ. US shale gas versus China’s coal as chemical feedstock. Environ Sci Technol 2015;49(16):9501–2.
CrossRef Google scholar
[8]
Ding J, Hua W. Game changers of the C3 value chain: Gas, coal, and biotechnologies. Chem Eng Technol 2013;36(1):83–90.
CrossRef Google scholar
[9]
New ExxonMobil and Saudi Aramco technologies produce ethylene directly from crude oil, cutting refining costs, IHS says [Interent]. London: IHS Markit; 2016 Jul 6 [cited 2016 Dec 16].Available from: http://news.ihsmarkit.com/press-release/new-exxonmobil-and-saudi-aramco-technologies-produce-ethylene-directly-crude-oil-cutti.
[10]
Al-Salem S, Lettieri P, Baeyens J. Recycling and recovery routes of plastic solid waste (PSW): A review. Waste Manag 2009;29(10):2625–43.
CrossRef Google scholar
[11]
Al-Salem S, Lettieri P, Baeyens J. The valorization of plastic solid waste (PSW) by primary to quaternary routes: From re-use to energy and chemicals. Prog Energ Combust 2010;36(1):103–29.
CrossRef Google scholar
[12]
Bridgwater AV. Review of fast pyrolysis of biomass and product upgrading. Biomass Bioenerg 2012;38:68–94.
CrossRef Google scholar
[13]
Putro JN, Soetaredjo FE, Lin SY, Ju YH, Ismadji S. Pretreatment and conversion of lignocellulose biomass into valuable chemicals. RSC Adv 2016;6(52):46834–52.
CrossRef Google scholar
[14]
Van Geem KM, Reyniers MF, Marin GB. Challenges of modeling steam cracking of heavy feedstocks. Oil Gas Sci Technol‒Rev IFP 2008;63(1):79–94.
CrossRef Google scholar
[15]
Nizamoff AJ. Renewable liquids as steam cracker feedstocks, PERP09/10S12.White Plains: Nexant, Inc.; 2010 Oct.
[16]
Foster J. Platts special report: Petrochemicals. Can shale gale save the naphtha crackers?London: Platts; 2013 Jan.
[17]
Longden R. INEOS Europe and Evergas enter into long-term shipping agreements [Internet]. Rolle: INEOS Olefins and Polymers Europe; 2013 Jan 23 [cited 2016 Dec 16]. Available from: http://www.ineos.com/news/shared-news/ineos-europe-and-evergas-enter-into-long-term-shipping-agreements/.
[18]
Tullo AH. Ethane supplier to the world—Chemical makers on three continents are set to tap into cheap feedstock from the US. Chem Eng News 2016; 94(44):28–9.
[19]
Pang P. Unconventional feedstocks to increase China’s clout in global chemical markets [Interent]. London: IHS Markit; 2014 May 20 [cited 2016 Dec 16]. Available from: http://blog.ihs.com/q12-unconventional-feedstocks-to-increase-chinas-clout-in-global-chemical-markets.
[20]
Plotkin JS. The propylene gap: How can it be filled? Washington, DC: American Chemical Society; 2015 Sep.
[21]
Kumar S, Panda AK, Singh R K. A review on tertiary recycling of high-density polyethylene to fuel. Resour Conserv Recy 2011;55(11):893–910.
CrossRef Google scholar
[22]
Garforth AA, Ali S, Hernández-Martínez J, Akah A. Feedstock recycling of polymer wastes. Curr Opin Solid St M 2004;8(6):419–25.
CrossRef Google scholar
[23]
Kee RJ, Karakaya C, Zhu H. Process intensification in the catalytic conversion of natural gas to fuels and chemicals. P Combust Inst 2017;36(1):51–76.
CrossRef Google scholar
[24]
Spath PL, Dayton DC. Preliminary screening; Technical and economic assessment of synthesis gas to fuels and chemicals with emphasis on the potential for biomass-derived syngas. Technical report. Golden: National Renewable Energy Laboratory; 2003 Dec. Report No.: NREL/TP-510-34929. DOE Contract No.: AC36-99-GO10337.
[25]
Stöcker M. Methanol-to-hydrocarbons: Catalytic materials and their behavior. Micropor Mesopor Mat 1999;29(1–2):3–48.
CrossRef Google scholar
[26]
Dry ME. High quality diesel via the Fischer–Tropsch process—A review. J Chem Technol Biot 2002;77(1):43–50.
CrossRef Google scholar
[27]
Chang CD, Silvestri AJ. The conversion of methanol and other O-compounds to hydrocarbons over zeolite catalysts. J Catal 1977;47(2):249–59.
CrossRef Google scholar
[28]
Keil FJ. Methanol-to-hydrocarbons: Process technology. Micropor Mesopor Mat 1999;29(1–2):49–66.
CrossRef Google scholar
[29]
Chen JQ, Bozzano A, Glover B, Fuglerud T, Kvisle S. Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process. Catal Today 2005;106(1–4):103–7.
CrossRef Google scholar
[30]
Tian P, Wei Y, Ye M, Liu Z. Methanol to olefins (MTO): From fundamentals to commercialization. ACS Catal 2015;5(3):1922–38.
CrossRef Google scholar
[31]
Chen D, Moljord K, Holmen A. A methanol to olefins review: Diffusion, coke formation and deactivation on SAPO type catalysts. Micropor Mesopor Mat 2012;164:239–50.
CrossRef Google scholar
[32]
Dry ME. Fischer–Tropsch reactions and the environment. Appl Catal A‒Gen 1999;189(2):185–90.
CrossRef Google scholar
[33]
Schulz H. Short history and present trends of Fischer–Tropsch synthesis. Appl Catal A ‒ Gen 1999;186(1–2):3–12.
CrossRef Google scholar
[34]
Wood DA, Nwaoha C, Towler BF. Gas-to-liquids (GTL): A review of an industry offering several routes for monetizing natural gas. J Nat Gas Sci Eng 2012;9:196–208.
CrossRef Google scholar
[35]
Dry ME. The Fischer–Tropsch process: 1950–2000. Catal Today 2002;71(3–4):227–41.
CrossRef Google scholar
[36]
Cheng J, Hu P, Ellis P, French S, Kelly G, Lok CM. Some understanding of Fischer–Tropsch synthesis from density functional theory calculations. Top Catal 2010;53(5):326–37.
CrossRef Google scholar
[37]
Dry ME. Practical and theoretical aspects of the catalytic Fischer–Tropsch process. Appl Catal A‒Gen 1996;138(2):319–44.
CrossRef Google scholar
[38]
Torres Galvis HM, Bitter JH, Khare CB, Ruitenbeek M, Dugulan AI, de Jong KP. Supported iron nanoparticles as catalysts for sustainable production of lower olefins. Science 2012;335(6070):835–8.
CrossRef Google scholar
[39]
Torres Galvis HM, de Jong KP. Catalysts for production of lower olefins from synthesis gas: A review. ACS Catal 2013;3(9):2130–49.
CrossRef Google scholar
[40]
Kondratenko EV, Baems M. Oxidative Coupling of Methane. In:Ertl G,KnözingerH, Schüth F, Weitkamp J, editors Handbook of heterogeneous catalysis. Weinheim: Wiley-VCH Verlag GmbH & Co. KGaA; 2008. p. 3010–23.
CrossRef Google scholar
[41]
Kondratenko EV, Schlüter M, Baerns M, Linke D, Holena M. Developing catalytic materials for the oxidative coupling of methane through statistical analysis of literature data. Catal Sci Technol 2015;5(3):1668–77.
CrossRef Google scholar
[42]
Olivos-Suarez AI, Szécsényi À, Hensen EJM, Ruiz-Martinez J, Pidko EA, Gascon J. Strategies for the direct catalytic valorization of methane using heterogeneous catalysis: Challenges and opportunities. ACS Catal 2016;6(5):2965–81.
CrossRef Google scholar
[43]
Keller GE, Bhasin MM. Synthesis of ethylene via oxidative coupling of methane: I. Determination of active catalysts. J Catal 1982;73(1):9–19.
CrossRef Google scholar
[44]
Galadima A, Muraza O. Revisiting the oxidative coupling of methane to ethylene in the golden period of shale gas: A review. J Ind Eng Chem 2016;37:1–13.
CrossRef Google scholar
[45]
Jašo S, Arellano-Garcia H, Wozny G. Oxidative coupling of methane in a fluidized bed reactor: Influence of feeding policy, hydrodynamics, and reactor geometry. Chem Eng J 2011;171(1):255–71.
CrossRef Google scholar
[46]
Mleczko L, Pannek U, Niemi VM, Hiltunen J. Oxidative coupling of methane in a fluidized-bed reactor over a highly active and selective catalyst. Ind Eng Chem Res 1996;35(1):54–61.
CrossRef Google scholar
[47]
Karakaya C, Kee RJ. Progress in the direct catalytic conversion of methane to fuels and chemicals. Prog Energ Combust 2016;55:60–97.
CrossRef Google scholar
[48]
Xu M, Lunsford JH. Effect of temperature on methyl radical generation over Sr/La2O3catalysts. Catal Lett 1991;11(3–6):295–300
CrossRef Google scholar
[49]
Feng Y, Niiranen J, Gutman D. Kinetic studies of the catalytic oxidation of methane. 1. Methyl radical production on 1% Sr/La2O3. J Phys Chem 1991;95(17):6558–63.
CrossRef Google scholar
[50]
Taylor RP, Schrader GL. Lanthanum catalysts for CH4 oxidative coupling: A comparison of the reactivity of phases. Ind Eng Chem Res 1991;30(5):1016–23.
CrossRef Google scholar
[51]
Tang L, Yamaguchi D, Wong L, Burke N, Chiang K. The promoting effect of ceria on Li/MgO catalysts for the oxidative coupling of methane. Catal Today 2011;178(1):172–80.
CrossRef Google scholar
[52]
Ito T, Wang J, Lin CH, Lunsford JH. Oxidative dimerization of methane over a lithium-promoted magnesium oxide catalyst. J Am Chem Soc 1985;107(18):5062–8.
CrossRef Google scholar
[53]
Arndt S, Simon U, Heitz S, Berthold A, Beck B, Görke O, et al.Li-doped MgOfrom different preparative routes for the oxidative coupling of methane. Top Catal 2011;54(16):1266–85.
CrossRef Google scholar
[54]
Myrach P, Nilius N, Levchenko SV, Gonchar A, Risse T, Dinse KP, et al.Temperature-dependent morphology, magnetic and optical properties of Li-doped MgO. Chem Cat Chem 2010;2(7):854–62.
CrossRef Google scholar
[55]
Hiyoshi N, Ikeda T. Oxidative coupling of methane over alkali chloride–Mn–Na2WO4/SiO2 catalysts: Promoting effect of molten alkali chloride. Fuel Process Technol 2015;133:29–34.
CrossRef Google scholar
[56]
Elkins TW, Hagelin-Weaver HE. Characterization of Mn–Na2WO4/SiO2 and Mn–Na2WO4/MgO catalysts for the oxidative coupling of methane. Appl Catal A‒Gen 2015;497:96–106.
CrossRef Google scholar
[57]
Koirala R, Büchel R, Pratsinis SE, Baiker A. Oxidative coupling of methane on flame-made Mn–Na2WO4/SiO2: Influence of catalyst composition and reaction conditions. Appl Catal A‒Gen 2014;484:97–107.
CrossRef Google scholar
[58]
Huang P, Zhao Y, Zhang J, Zhu Y, Sun Y. Exploiting shape effects of La2O3nanocatalysts for oxidative coupling of methane reaction. Nanoscale 2013;5(22):10844–8.
CrossRef Google scholar
[59]
Hou YH, Han WC, Xia WS, Wan HL. Structure sensitivity of La2O2CO3catalysts in the oxidative coupling of methane. ACS Catal 2015;5(3):1663–74.
CrossRef Google scholar
[60]
Song J, Sun Y, Ba R, Huang S, Zhao Y, Zhang J, et al.Monodisperse Sr–La2O3 hybrid nanofibers for oxidative coupling of methane to synthesize C2 hydrocarbons. Nanoscale 2015;7(6):2260–4.
CrossRef Google scholar
[61]
Scher EC, Cizeron JM, Schammel WP, Tkachenko A, Gamoras J, Karshtedt D, et al., inventors; Siluria Technologies, Inc., assignee. Method for the oxidative coupling of methane in the presence of a nanowire catalyst. European Patent EP 2853521 A1. 2015 Apr 1.
[62]
Schammel WP, Wolfenbarger J, Ajinkya M, Mccarty J, Cizeron JM, Weinberger S, et al., inventors; Siluria Technologies, Inc., assignee. Oxidative coupling of methane systems and methods. PCT Patent WO 2013177433 A2. 2013 Nov 28.
[63]
Zohour B, Noon D, Senkan S. New insights into the oxidative coupling of methane from spatially resolved concentration and temperature profiles. Chem Cat Chem 2013;5(10):2809–12.
CrossRef Google scholar
[64]
Horn R, Williams K A, Degenstein N J, Schmidt L D. Syngas by catalytic partial oxidation of methane on rhodium: Mechanistic conclusions from spatially resolved measurements and numerical simulations. J Catal 2006;242(1):92–102.
CrossRef Google scholar
[65]
Donazzi A, Maestri M, Michael BC, Beretta A, Forzatti P, Groppi G, et al.Microkinetic modeling of spatially resolved autothermal CH4 catalytic partial oxidation experiments over Rh-coated foams. J Catal 2010;275(2):270–9.
CrossRef Google scholar
[66]
Mleczko L, Baerns M. Catalytic oxidative coupling of methane—Reaction engineering aspects and process schemes. Fuel Process Technol 1995;42(2–3):217–48.
CrossRef Google scholar
[67]
Dautzenberg FM, Schlatter JC, Fox JM, Rostrup-Nielsen JR, Christiansen LJ. Catalyst and reactor requirements for the oxidative coupling of methane. Catal Today 1992;13(4):503–9.
CrossRef Google scholar
[68]
Sattler JJ, Gonzalez-Jimenez ID, Luo L, Stears BA, Malek A, Barton DG, et al.Platinum-promoted Ga/Al2O3 as highly active, selective, and stable catalyst for the dehydrogenation of propane. Angew Chem 2014;126(35):9405–10.
CrossRef Google scholar
[69]
Ren T, Daniëls B, Patel MK, Blok K. Petrochemicals from oil, natural gas, coal and biomass: Production costs in 2030–2050. Resour Conserv Recy 2009;53(12):653–63.
CrossRef Google scholar
[70]
Naims H. Economics of carbon dioxide capture and utilization—A supply and demand perspective. Environ Sci Pollut Res Int 2016;23(22):22226–41.
CrossRef Google scholar
[71]
Leung DYC, Caramanna G, Maroto-Valer MM. An overview of current status of carbon dioxide capture and storage technologies. Renew Sustain Energy Rev 2014;39:426–43.
CrossRef Google scholar
[72]
Weikl MC, Schmidt G. Carbon capture in cracking furnaces. In: Proceedings of theAIChE 2010 Spring Meeting and the 6th Global Congress on Process Safety; 2010 Mar 21–25; San Antonio, USA; 2010.

Acknowledgements

This work was supported by the Long-Term Structural Methusalem Funding (BOF09/01M00409) by the Flemish Government and the European Union’s Horizon H2020 Programme (H2020-SPIRE-04-2016) under grant agreement No. 723706. Ismaël Amghizar acknowledges financial support from SABIC Geleen. Laurien A. Vandewalle acknowledges financial support from a doctoral fellowship from the Fund for Scientific Research, Flanders (FWO).

Compliance with ethics guidelines

Ismaël Amghizar, Laurien A. Vandewalle, Kevin M. Van Geem, and Guy B. Marin declare that they have no conflict of interest or financial conflicts to disclose.
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2017 2017 THE AUTHORS. Published by Elsevier LTD on behalf of the Chinese Academy of Engineering and Higher Education Press Limited Company. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
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