Effect of Temperature on Gas and Liquid Products Distribution in Thermal Cracking of Nigerian Bitumen
DOI:
https://doi.org/10.31699/IJCPE.2021.2.2Keywords:
Agbabu bitumen, Petrochemicals, Cracking, Steel reactorAbstract
The increasing population growth resulting in the tremendous increase in consumption of fuels, energy, and petrochemical products and coupled with the depletion in conventional crude oil reserves and production make it imperative for Nigeria to explore her bitumen reserves so as to meet her energy and petrochemicals needs. Samples of Agbabu bitumen were subjected to thermal cracking in a tubular steel reactor operated at 10 bar pressure to investigate the effect of temperature on the cracking reaction. The gas produced was analyzed in a Gas Chromatograph while the liquid products were subjected to Gas Chromatography-Mass Spectrometry (GC-MS) analysis. Heptane was the dominant gas produced in bitumen cracking at all temperatures and the reaction products show a distribution of lighter hydrocarbons most of which are in the gasoline range. The product distribution of bitumen conversion depends strongly on the cracking temperature and the oil produced contains the valuable liquid fractions. The products of thermal cracking of bitumen can be classified into the following groups; alkanes, alkenes, amines, aromatics, alkanoic acids, alkanols, esters, ethers, ketones, sulphur compounds, and nitrogen compounds. The activation energies of the products formed were determined. The LNG produced all have unusually low values activation energy (hence easily converted) pointing to the high quality of Agbabu crude
The conversion process was affected by the reaction time and suggests that the transformation of bitumen into smaller fractions follows a definite reaction scheme in which the heavy oil transformed to lower fractions and was subsequently converted to smaller liquid fractions and gases.
Received on 04/04/2021
Accepted on 19/06/2021
Published on 30/06/2021
References
Stosur, G. J., Waisley S. L., Reid T. B., and Marchant L. C. (1998) “Tar Sands – Technology, Economics and Environmental Issues for Commercial Production beyond the 2000”, Paper No 1998-002 presented at the 7th. UNITAR International Conference on Heavy Oil and Tar Sand, Beijing, China, 27-30th October, 11-18.
Chen, Z. J. (2006) Heavy Oils Part I. SIAM News, 39, 3.
Adegoke, O.S., Ako, B.S., Enu, E.I., Afonja, A.A., Ajayi, T.R., Enufurieta, W.O., Jeje, L.K., Dogoke –Anthony, C.W., Omatshola, M.E and Rahaman, M.A (1989).“The Tar sands of Ondo State’’ A brochure was prepared for the state visit by the President and Commander-in-Chief of Armed forces of the Fed.Rep. of Nigeria. pp 6-26.
Coker, S.J.L. (1988) “Bitumen saturation and reserve: Estimate of Okitipupa oil sand”.Nigeria Journal of Mining Geology. 38: 1-2.
Obiajunwa, E.I.,and Nwachukwu,J.I.(2000). “Simultaneous PIXE and PIGME analysis of a Nigerian tar sand sample from a deep borehole”.J.Radio Anal.Nucl.Chem.245:659-661.
Adegoke, O.S., and Ibe, E.C. (1982): "The Tar Sand and Heavy Crude Resources of Nigeria", Proceedings of 2nd International Conference on Heavy Crudes and Tar Sand.Caracas, Venezuela. pp. 280-285.
Bello, O.O., Sonibare, J.A., Ademodi, B.T., Macaulay, S.R.A. and Adebiyi, F.M. (2003) “Environmental Impact Assessment of commercial Tar Sands Development in Nigeria”,NAFTA Croatia, 54 (11), pp.417-423
Egloff. C. and Morrell, J. C. (1926) “Systematic Refining of Cracked Distillates” Trans. Am. Inst. Chem. Eng., 18, 347.
Egloff, C. and Morrell. J. C.(1927) “Cracking of Bitumen derived from Alberta Tar sands .” Can. Chem. Metall. 11,33.
Burger, J. W., Cogswell, D. E. and Oblad, A. G. (1977) “Thermal Processing of a Utah Tar Sand Bitumen”, The Oil Sands of Canada-Venezuela Symposium, CIM Publication.17. 178 182.
Hayashitani. M.. Bennion, D. W.. Donnelly, J. K. and Moore, R. G. (1977). Proc. Oil Sands of Canada-Venezuela Symp. CIM Special Publication. 17. 233
Hayashitani, M. (1978) ‘Thermal Cracking of Athabasca Bitumen’, PhD Thesis, University of Calgary,Calgary, Canada.
Magaril, R. Z. and Axenova E. I., (1970) Oil Gas J.5. 47.
Speight, J.G. (1970) “Thermal cracking of Athabasca bitumen, Athabasca asphaltenes, and Athabasca deasphalted heavy oil”, Fuel, 49, 134-145.
Rahimi, P., Dettman, H., Gentzis, T., Chung, K. and Nowlan,V.(1997a).“Upgrading chemistry of Athabasca bitumen fractions derived by super critical fluid extraction”, Presented at the 47th CSChE conference, Edmonton, Alberta, Canada, October 5-8.
Rahimi, P., Dettman, H., Nowlan, V. and DelBianco, A.(1997b). “Molecular transformation during heavy oil upgrading”, Prep. Div. Pet. Chem., American Chemical Society, National Meeting, San Francisco, CA, April 13-17; 23-26.
Rahimi, P.M., Parker, R.J., Hawkins, R., Gentzis, T. and Tsaprailis, H.(2001) “Processability of partially deasphated Athabasca bitumen”, Prep. Div. Pet. Chem., American Chemical Society, National Meeting, San Diego, CA., April 1-5, 74-77.
Yasar, M., Trauth, D.M. and Klein, M.T.(1992). “Asphaltene and resid pyrolysis 2: The effect of reaction environment on pathways and selectivities”, Prep. Div. Fuel Chem., American Chemical Society, National Meeting, Washington, D.C., August 23-2;pp. 1878-1885.
Dawson, W.H., Chornet, E., Tiwari, P. and Heitz, M. (1989). Hydrocracking of individual components isolated from Athabasca bitumen vacuum resid, Prep. Div. of Pet.Chem.,American Chemical Society, National Meeting, Dallas, TX, April 9-14; 34(2), 384- 394.
Liu, C., Zhu, C., Jin, L., Shen, R.and Liang, W. (1999).Step by step modeling for thermal reactivities and chemical compositions of vacuum residues and their SFEF asphalts, Fuel Process. Technol.,59, 51-67.
Eshraghian A and Husein M.M., (2017) “Thermal Cracking of Athabasca Vacuum Residue and Bitumen and Their Maltene Fraction in a Closed Reactor System,” Fuel, vol. 190, pp. 396-408.
Isnandar Yunanto, Sri Haryati and Muhammad Djoni Bustan (2019) “Pyrolysis of Vacuum Residue By Thermal and Catalytic Cracking Using Active Alumina Catalyst” Indones. J. Fundam. Appl. Chem., 4(1), 2019, 29-34. DOI: 10.24845/ijfac.v4.i1.29
Jin Huo, Shuai Zhao, Jingjun Pan, Wanfen Pu, Mikhail A.Varfolomeev, Dmitrii A. Emelianov.(2021) “Evolution of mass losses and evolved gases of crude oil and its SARA components during low-temperature oxidation by isothermal TG–FTIR analyses”. Journal of Thermal Analysis and Calorimetry, 667 https://doi.org/10.1007/s10973-021-10841-z
Chengdong Yuan, Dmitrii A. Emelianov, Mikhail A. Varfolomeev. (2018) “Oxidation Behavior and Kinetics of Light, Medium, and Heavy Crude Oils Characterized by Thermogravimetry Coupled with Fourier Transform Infrared Spectroscopy”. Energy & Fuels, 32 (4) , 5571-5580. https://doi.org/10.1021/acs.energyfuels.8b00428
Shuai Zhao, Wanfen Pu, Mikhail A. Varfolomeev, Chengdong Yuan, Alexander A. Rodionov. (2019) “Integrative Investigation of Low-Temperature Oxidation Characteristics and Mechanisms of Heavy Crude Oil”. Industrial & Engineering Chemistry Research, 58 (31) , 14595-14602. https://doi.org/10.1021/acs.iecr.9b03346
Atkins, L., (2011). Heavy crude oil: A global analysis and outlook, available at www.heavyoilinfo.com/feature-items/heavy-crude-oil-a-global-analysis-and-outlook, accessed 23/08/2015.
Islas-Flores, C.A.,Buenrostro-Gonzalez,E. and Lira-Galeana,E.(2005).“Comparison between Open Column Chromatography and HPLC SARA fractionations in Petroleum”.Energy and Fuels 19(5), 2080-2088.
Martinez-Grimaldo, H., Ortiz-Moreno, Hugo., Sanchez-Minero, F., Ramirez, Jorge., Cuevas-Garcia, Rogelio., and Ancheyta-Juarez, Jorge.(2014) “Hydrocracking of Maya crude oil in a slurry-phase reactor.1.Effect of reaction temperature”. Catalysis Today. 220-222, 295- 300.
Gates, C. B., James, R. Katzer and G.C.A. Schuit (1979) “Chemistry of Catalytic Processes MC”. Graw-Hill Series in Chemical Engineering.
Satterfield, C.N (1980). “Heterogeneous Catalysis in Practice”. McGraw Hill, pp. 238-242.
Speight, J. G., (2011). “The refinery of the future”. Gulf Professional Publishing London,pp 81- 116
Sawarkar, A.N., Pandit, A.B., and Joshi, J.B.(2007)“Studies in Coking of Arabian mix Vacuum Residue”. Chemical Engineering Research and Design,85(A4):481-491.
Kim, J. –W., Longstaff, C. D., Hanson, V. F., (1998). “Catalytic and thermal effects during hydrotreating of bitumen-derived heavy oil”, Fuel, 77 (15), 1815.
Kressmann, S., More, F., Harle, V., Kasztelan, S., (1998). “Recent development in fixed-bed catalytic residue upgrading”, Catalysis Today, 43, 203-215.
Lee, H. J., Kang, S., Kim, Y. and Park, S. (2011). “New approach for kinetic modeling of catalytic cracking of paraffinic naphtha”. Industrial & Engineering Chemistry Research, 50, 4264-4279.
Beaton, W.I. and Bertolacini, R.J., (1991) “Resid Hydroprocessing at Amoco”, Catalysis Reviews- Science and Engineering, 33 (3-4), 281-317.
Parsons, A. F (2000) “An introduction to free radical chemistry’ Blackwell Science;York.
Galarraga, Carmen E. , Carlos Scott, Herbert Loria, and Pedro Pereira-Almao.(2012) “Kinetic Models for Upgrading Athabasca Bitumen Using Unsupported NiWMo Catalysts at Low Severity Conditions”. Ind. Eng. Chem. Res. 51, 140–146 dx.doi.org/10.1021/ie201202b.
Sanchez, S.; Rodriguez, M. A.; Ancheyta, J.(2005) “Kinetic model for moderate hydrocracking of heavy oils”. Ind. Eng. Chem. Res. 44, 9409.
Fumoto, E.; Matsumara, A.; Sato, S.; Takanohashi, (2010) “Oxidative cracking of residual oil with iron oxide catalyst in a steam atmosphere”. Prepr. - Am. Chem. Soc., Div. Pet. Chem 50,50.
Barbour, R. V., Dorrence, S. M., Vollmer, T. L. and Harris, J. D. (1976) ‘Pyrolysis of Utah Tar Sands, Products and Kinetics’, presented at CONFAB 1976. University of Wyoming Science, Camp, USA. 19.-24 July.
Ebrahimi, S., J.S. Moghaddas , and M.K. Razavi Aghjeh(2008) ‘Study on thermal cracking behavior of petroleum residue’Fuel 87 : 1623–1627.
Al Soufi HH, Savaya ZF, Moahummed HK, Al-Azami IA.(1988) “Thermal conversion (visbreaking) of heavy Iraqi residue”. Fuel 67:1714–5.
Singh J, Kumar MM, Saxena AK, Kumar S.(2004) “Studies on thermal cracking behavior of residual feedstocks in a batch reactor”. Chem Eng Sci.59:4505–15.
Marsh H, Martinez-Escandell M, Rodriguez-Reinoso F.(1999) “Semicokes from pitch pyrolysis: mechanisms and kinetics”. Carbon.37:363–90.
Vyazovkin S. (2003) “Reply to ‘what is meant by the term ‘variable activation energy’ when applied in the kinetics analyses of solid state decompositions (crystolysis reactions)?”.Thermochim Acta.397(1-2)269-71.
Nashaat N.Nassar, Azfar Hassan,German Luna and Pedro Pereira-Almao(2013) “Comparative study on thermal cracking of Athabasca bitumen” J Therm Anal Calorim 114:465-472.
Strausz. O.P., Kamal N.Jha and Douglas S.Montgomery(1977) “Chemical composition of gases in Athabasca bitumen and in low-temperature thermolysis of oil sand, asphaltene and maltene” Fuel 56:114-120.
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