GTL Process Simulation and Sensitivity Analysis: Zero CO2 Emission and Productivity Improvement

Document Type : Research Article

Authors

1 Urmia University of Technology

2 Chemical Engineering, Urmia University of Technology

Abstract

Refineries and petrochemical industries can transform some of their flare gas into noteworthy gasoil, gasoline, and LPG products by applying technology of Gas-to-Liquid (GTL). One of the main parts of GTL plant is the production of synthetic gas process. As the main objective of this study, two technology steam methane reforming (SMR) and tri-methane reforming (TMR) techniques have been used to simulate and analyze the proposed sensitivity of the new integrated GTL process. Therefore, four parameters have been studied in sensitivity analysis against changing the proportion of gas recovery to gas synthesis and amine subunits. Therefore, four parameters have been studied in sensitivity analysis (SA) against changing the proportion of gas recovery to gas synthesis and amine subunits. SA results represented that raising recycle gas ratio has negative impact on SMR model productivity and has positive effect on TMR model productivity, especially between 0.0 to 0.7 ratios. Also, the decreasing trend of the syngas production rate in the SMR was much more severe and with a greater slope than the increase in the syngas production rate in the TMR. Therefore, on this basis, the final productivity in the integrated process also shows a significant increase about by using the TMR process (3835 kg/hr.) versus the SMR process (3793 kg/hr.).

Highlights

  • Sensitivity analysis results represented that increasing the recycle gas ratio has a negative effect on SMR productivity and a positive effect on TMR productivity
  • Some advantages of the TMR process compared with other well-known types of reforming processes are Higher energy efficiency, control of synthesis gas ratio (H2/CO), and minimizing coke formation.
  • The rate of productivity decline is more severe in SMR model by increasing recycle ratio of recycled gas.

Keywords


[1]  Al-Sobhi, S.A., Alnouss, A., Alhamad, M., 2021. Techno-economic and environmental assessment of gasoline produced from GTL and MTG processes, Computer Aided Chemical Engineering, 50, 1827-1832. https://doi.org/10.1016/B978-0-323-88506-5.50283-7
[2]  Al-Yaeeshi, A.A., Alnouss, A., Mckay, G., Al-Ansari, T., 2020. A simulation study on the effect of CO2 injection on the performance of the GTL process. Computers & Chemical Engineering, 136, 106768-106778. https://doi.org/10.1016/j.compchemeng.2020.106768
[3]  Anchieta, C.G., Assaf, E.M., Assaf, J.M., 2019. Effect of ionic liquid in Ni/ZrO2 catalysts applied to syngas production by methane tri-reforming, International Journal of Hydrogen Energy, 44 (18), 9316-9327. https://doi.org/10.1016/j.ijhydene.2019.02.122
[4]  Arab Aboosadi, Z., Jahanmiri, A.H., Rahimpour, M.R., 2011. Optimization of tri-reformer reactor to produce synthesis gas for methanol production using differential evolution (DE) method, Applied Energy, 88 (8), 2691-2701. http://dx.doi.org/10.1016/j.apenergy.2011.02.017
[5]  Behroozsarand, A. and Zamaniyan, A., 2017. Simulation and optimization of an integrated GTL process. Journal of Cleaner Production, 142 (4), 2315-2327. https://doi.org/10.1016/j.jclepro.2016.11.045
[6]  Chein, R.Y., Hsu, W.H., 2018. Thermodynamic analysis of syngas production via tri-reforming of methane and carbon gasification using flue gas from coal-fired power plants, Journal of Cleaner Production, 200, 242-258. https://doi.org/10.1016/j.jclepro.2018.07.228
[7]  Chein, R.Y., Wang, C.Y., Yu, C.T., 2017. Parametric study on catalytic tri-reforming of methane for syngas production, Energy, 118, 1-17. http://dx.doi.org/10.1016/j.energy.2016.11.147
[8]  Chen, Q., Wang, D., Gu, Y., Yang, S., Tang, Z., Sun, Y., Wu, Q., 2020. Techno-economic evaluation of CO2-rich natural gas dry reforming for linear alpha olefins production, Energy Conversion and Management, 205, 112348-112359. https://doi.org/10.1016/j.enconman.2019.112348
[9]  Cho, W., Song, T., Mitsos, A., Mckinnon, J.T., Ko, G.H., Tolsma, J.E., Denholm, D., Park, T., 2009. Optimal design and operation of a natural gas tri-reforming reactor for DME synthesis. Catalysis Today 139 (4), 261-267. http://dx.doi.org/10.1016/j.cattod.2008.04.051
[10]         Damanabi, A.T., Servatan, M., Mazinani, S., Olabi, A.G., Zhang, Z., 2019. Potential of tri-reforming process and membrane technology for improving ammonia production and CO2 reduction, Science of The Total Environment, 664, 567-575. https://doi.org/10.1016/j.scitotenv.2019.01.391
[11]         Díez-Ramírez, J., Dorado, F., Martínez-Valiente, A., García-Vargas, J.M., and Sánchez, P., 2016. Kinetic, energetic and exergetic approach to the methane tri-reforming process. International Journal of Hydrogen Energy. http://dx.doi.org/10.1016/j.ijhydene.2016.04.229
[12]         Dwivedi, A., Gudi, R., Biswas, P., 2016. Sensitivity based optimization of the Tri-reforming based CO2 valorization process, IFAC-PapersOnLine, 49 (7), 359-364. http://dx.doi.org/10.1016/j.ifacol.2016.07.362
[13]         Dwivedi, A., Gudi, R., Biswas, P., 2020. An oxy-fuel combustion based tri-reforming coupled methanol production process with improved hydrogen utilization, International Journal of Greenhouse Gas Control, 93, 102905-102924. https://doi.org/10.1016/j.ijggc.2019.102905
[14]         Elsayed, N.H., Elwell, A., Joseph, B., Kuhn, J.N., 2017. Effect of silicon poisoning on catalytic dry reforming of simulated biogas. Applied Catalysis A: General, 538, 157-164. https://doi.org/10.1016/j.apcata.2017.03.024
[15]         Farniaei, M., Abbasi, M., Rahnama, H., Rahimpour, M.R., Shariati, A., 2014. Syngas production in a novel methane dry reformer by utilizing of tri-reforming process for energy supplying: Modeling and simulation, Journal of Natural Gas Science and Engineering, 20 (9), 132-146. http://dx.doi.org/10.1016/j.jngse.2014.06.010
[16]         Farsi, M., Fekri Lari, M., Rahimpour, M.R., 2019. Development of a green process for DME production based on the methane tri-reforming, Journal of the Taiwan Institute of Chemical Engineers, 106, 9-19. https://doi.org/10.1016/j.jtice.2019.10.001
[17]         Fedorova, Z.A., Danilova, M.M., Zaikovskii, V.I., 2020. Porous nickel-based catalysts for tri-reforming of methane to synthesis gas: Catalytic activity, Materials Letters, 261, 127087-127101. https://doi.org/10.1016/j.matlet.2019.127087
[18]         Gangadharan, P., Kanchi, K.C., Lou, H.H., 2012. Evaluation of the economic and environmental impact of combining dry reforming with steam reforming of methane, Chemical Engineering Research and Design, 90 (11) 1956-1968. http://dx.doi.org/10.1016/j.cherd.2012.04.008
[19]         García-Vargas, J.M., Valverde, J.L., De Lucas-Consuegra, A., Gómez-Monedero, B., Dorado, F., Sánchez, P., 2013. Methane tri-reforming over a Ni/β-SiC-based catalyst: Optimizing the feedstock composition, International Journal of Hydrogen Energy, 38 (11) 4524-4532. http://dx.doi.org/10.1016/j.ijhydene.2013.02.001
[20]         García-Vargas, J.M., Valverde, J.L., De Lucas-Consuegra, A., Gómez-Monedero, B., Sánchez, P., Dorado, F., 2012. Precursor influence and catalytic behaviour of Ni/CeO2 and Ni/SiC catalysts for the tri-reforming process, Applied Catalysis A: General, 431–432, 49-56. http://dx.doi.org/10.1016/j.apcata.2012.04.016
[21]         García-Vargas, J.M., Valverde, J.L., Díez, J., Dorado, F., Sánchez, P., 2015. Catalytic and kinetic analysis of the methane tri-reforming over a Ni–Mg/β-SiC catalyst, International Journal of Hydrogen Energy, 40 (28), 8677-8687. http://dx.doi.org/10.1016/j.ijhydene.2015.05.032
[22]         García-Vargas, J.M., Valverde, J.L., Díez, J., Sánchez, P., Dorado, F., 2014. Influence of alkaline and alkaline-earth cocations on the performance of Ni/β-SiC catalysts in the methane tri-reforming reaction, Applied Catalysis B: Environmental, 148–149, 322-329. http://dx.doi.org/10.1016/j.apcatb.2013.11.013
[23]         García-Vargas, J.M., Valverde, J.L., Díez, J., Sánchez, P., Dorado, F., 2015. Preparation of Ni–Mg/β-SiC catalysts for the methane tri-reforming: Effect of the order of metal impregnation, Applied Catalysis B: Environmental, 164 (3), 316-323. http://dx.doi.org/10.1016/j.apcatb.2014.09.044
[24]         Hernandez, B. Martin, M., 2018. Optimization for biogas to chemicals via tri-reforming. Analysis of Fischer-Tropsch fuels from biogas, Energy Conversion and Management, 174, 998-1013. https://doi.org/10.1016/j.enconman.2018.08.074
[25]         Hossain, M.A., Ayodele, B.V., Cheng, C.K., Khan, M.R., 2016. Artificial neural network modeling of hydrogen-rich syngas production from methane dry reforming over novel Ni/CaFe2O4 catalysts, International Journal of Hydrogen Energy, 41 (26), 11119-11130. http://dx.doi.org/10.1016/j.ijhydene.2016.04.034
[26]         Khajeh, S., Arab Aboosadi, Z., Honarvar, B., 2015. Optimizing the fluidized-bed reactor for synthesis gas production by tri-reforming, Chemical Engineering Research and Design, 94 (2), 407-416. http://dx.doi.org/10.1016/j.cherd.2014.08.018
[27]         Kozonoe, C.E., De Paiva Floro Bonfim, R., Brito Alves, R.M., Schmal, M., 2019. The Fe-Co-Cu supported on MWCNT as catalyst for the tri-reforming of methane – Investigating the structure changes of the catalysts, Fuel, 256, 115917-115930. https://doi.org/10.1016/j.fuel.2019.115917
[28]         Kumar, R., Kumar, K., Pant, K.K., and Choudary, N.V., 2020. Tuning the metal-support interaction of methane tri-reforming catalysts for industrial flue gas utilization, International Journal of Hydrogen Energy, 45 (3), 1911-1929. https://doi.org/10.1016/j.ijhydene.2019.11.111
[29]         Lee, S.H., Cho, W., Ju, W.S., Cho, B.H., Lee, Y.C., Baek, Y.S., 2003. Tri-reforming of CH4 using CO2 for production of synthesis gas to dimethyl ether, Catalysis Today, 87 (1–4), 133-137. http://dx.doi.org/10.1016/j.cattod.2003.10.005
[30]         Majewski, A.J. Wood, J., 2014. Tri-reforming of methane over Ni@SiO2 catalyst, International Journal of Hydrogen Energy, 39 (24), 12578-12585. http://dx.doi.org/10.1016/j.ijhydene.2014.06.071
[31]         Osat, M., Shojaati, F., Hafizi, A., 2022. Optimization and improvement of a conventional tri-reforming reactor to an energy efficient membrane reactor for hydrogen production, Chemical Engineering and Processing - Process Intensification, 175,  108933-108945. https://doi.org/10.1016/j.cep.2022.108933
[32]         Oyama, S.T., Hacarlioglu, P., Gu, Y., Lee, D., 2012. Dry reforming of methane has no future for hydrogen production: Comparison with steam reforming at high pressure in standard and membrane reactors, International Journal of Hydrogen Energy, 37 (13), 10444-10450. http://dx.doi.org/10.1016/j.ijhydene.2011.09.149
[33]         Pino, L., Vita, A., Cipitì, F., Laganà, M., Recupero, V., 2011. Hydrogen production by methane tri-reforming process over Ni–ceria catalysts: Effect of La-doping, Applied Catalysis B: Environmental, 104 (1–2), 64-73. http://dx.doi.org/10.1016/j.apcatb.2011.02.027
[34]         Pino, L., Vita, A., Laganà, M., Recupero, V., 2014. Hydrogen from biogas: Catalytic tri-reforming process with Ni/LaCeO mixed oxides, Applied Catalysis B: Environmental, 148–149, 91-105. http://dx.doi.org/10.1016/j.apcatb.2013.10.043
[35]         Rahnama, H., Farniaei, M., Abbasi, M., Rahimpour, M.R., 2014. Modeling of synthesis gas and hydrogen production in a thermally coupling of steam and tri-reforming of methane with membranes, Journal of Industrial and Engineering Chemistry, 20 (4), 1779-1792. http://dx.doi.org/10.1016/j.jiec.2013.08.032
[36]         Sadeghi, M., Jafari, M., Yari, M., Mahmoudi, S.M.S., 2018. Exergoeconomic assessment and optimization of a syngas production system with a desired H2/CO ratio based on methane tri-reforming process, Journal of CO2 Utilization, 25, 283-301. https://doi.org/10.1016/j.jcou.2018.04.009
[37]         Saebea, D., Authayanun, S., Arpornwichanop, A., 2019. Process simulation of bio-dimethyl ether synthesis from tri-reforming of biogas: CO2 utilization, Energy, 175, 36-45. https://doi.org/10.1016/j.energy.2019.03.062
[38]         Schmal, M., Toniolo, F.S., Kozonoe, C.E., 2018. Perspective of catalysts for (Tri) reforming of natural gas and flue gas rich in CO2, Applied Catalysis A: General, 568, 23-42. https://doi.org/10.1016/j.apcata.2018.09.017
[39]         Si, L.-J., Wang, C.-Z., Sun, N.-N., Wen, X., Zhao, N., Xiao, F.-K., Wei, W., Sun, Y.-H., 2012. Influence of preparation conditions on the performance of Ni-CaO-ZrO2 catalysts in the tri-reforming of methane, Journal of Fuel Chemistry and Technology, 40 (2), 210-215. http://dx.doi.org/10.1016/S1872-5813(12)60011-5
[40]         Song, C. Pan, W., 2004. Tri-reforming of methane: a novel concept for catalytic production of industrially useful synthesis gas with desired H2/CO ratios, Catalysis Today, 98 (4), 463-484. http://dx.doi.org/10.1016/j.cattod.2004.09.054
[41]         Wu, W., Yang, H.T., Hwang, J.J., 2014. Conceptual design of syngas production systems with almost net-zero carbon dioxide emissions, Energy, 74, 753-761. http://dx.doi.org/10.1016/j.energy.2014.07.042
[42]         Yoo, J., Bang, Y., Han, S.J., Park, S., Song, J.H., Song, I.K., 2015. Hydrogen production by tri-reforming of methane over nickel–alumina aerogel catalyst, Journal of Molecular Catalysis A: Chemical, 410, 74-80. http://dx.doi.org/10.1016/j.molcata.2015.09.008
[43]         Zhang, Y., Cruz, J., Zhang, S., Lou, H.H., Benson, T.J., 2013. Process simulation and optimization of methanol production coupled to tri-reforming process, International Journal of Hydrogen Energy, 38 (31), 13617-13630. http://dx.doi.org/10.1016/j.ijhydene.2013.08.009
[44]         Zhang, Y., Zhang, S., Benson, T., 2015. A conceptual design by integrating dimethyl ether (DME) production with tri-reforming process for CO2 emission reduction, Fuel Processing Technology, 131 (3), 7-13. http://dx.doi.org/10.1016/j.fuproc.2014.11.006