Catalytic Activity of Synthesized NiMo Catalysts on Walnut Shell Activated Carbon for Heavy Naphtha Hydrotreating

Document Type : Research Article

Authors

School of Chemistry, College of Science, University of Tehran, Tehran, I.R. IRAN

Abstract

Hydrotreating heavy naphtha using highly active NiMo catalysts on walnut shell activated carbon (NiMo-WAC) nanocatalysts is a new technology for clean fuel production. In this research, pyrolysis of the walnut shell as a scalable, low-cost, and high-yield method was used to synthesize chemically activated carbon in the presence of ZnCl2, as activating agent. To enhance the catalytic conversion, walnut shell active carbon was functionalized with HCL, HNO3, and H2SO4 to prepare NiMo-WAC1, NiMo-WAC2, and NiMo-WAC3 respectively. These nanocatalysts were synthesized through the incipient wetness impregnation method and characterized by X-Ray Diffraction (XRD), Fourier Transform InfraRed (FT-IR) spectroscopy, Inductively Coupled Plasma-atomic emission (ICP) spectroscopy, Field Emission Scanning Electron Microscopy (FESEM), Brunauer–Emmett–Teller (BET) surface area, Temperature-Programmed Desorption (TPD) and Temperature-Programmed Reduction (TPR) techniques. CHNS (Eager 300 for EA1112) was used to study elemental analysis of the walnut shell feedstock used for active carbon synthesis. Different operating parameters including temperature, pressure, LHSV, and H2/feed (heavy naphtha) ratio for hydrodesulfurization (HDS) reactions were explored by evaluating NiMo-WAC nanocatalysts catalytic activity. HDS of heavy naphtha with 2491 ppm of sulfur in the operation condition of temperature: 290 °C, pressure: 30 bar, H2/oil: 100 NL/L, and LHSV: 3.3 h-1 showed considerably higher activity of NiMo-WAC2 nanocatalyst, less than 10 ppm in the product, than NiMo-γAl2O3 as a commercial and reference catalyst, maximum 104 ppm in the product, and this is economically valuable.

Keywords

Main Subjects


[1] Abubakar U.C., Alhooshani K.R., Saleh T.A., Effect of Ultrasonication and Chelating Agents on the Dispersion of Nimo Catalysts on Carbon for Hydrodesulphurization., J. Environ. Chem. Eng., 8: 1–6 (2020).
[3] Padervand M., Lammel G., Bargahi A., Mohammad-Shiri H., Photochemical Degradation of the Environmental Pollutants over the Worm-Like Nd2 CuO4 -Nd2O3 Nanostructures, Nano-Structures and Nano-Objects, 18: 100258 (2019).
[4] Padervand M., Gholami M.R., Removal of Toxic Heavy Metal Ions from Waste Water by Functionalized Magnetic Core-Zeolitic Shell Nanocomposites as Adsorbents, Environ. Sci. Pollut. Res., 20: 3900–3909 (2013).
[5] Heidari Samiromi A., Jahangiri A.R., Investigation of CO2 Solubility in Blends of AMP and HMDA Solvents: Thermodynamic Modeling Based on the Deshmukh-Mather Model, Iran. J. Chem. Chem. Eng. (IJCCE), 40(1): 231–240 (2021).
[6]    Alinezhad H., Fakhimi Abarghouei M.R., Tajbakhsh M., Niknam K., Application of Mea, Tepa, and Morpholine Grafted Nay Zeolite as CO2 Capture, Iran. J. Chem. Chem. Eng., 40(2): 581–592 (2021).
[8]    Ebrahiminejad M., Karimzadeh R., Hydrocracking and Hydrodesulfurization of Diesel Over Zeolite Beta-Containing NiMo Supported on Activated Red Mud, Adv. Powder. Technol., 30: 1450–1461 (2019).
[9]    Sheibani S., Zare K., Mousavi Safavi S.M.., The Effects of pH and Chelating Agent on Synthesis and Characterization of NI mo/γ- Alumina Nanocatalyst for Heavy Oil Hydrodesulfurization, Iran. J. Chem. Chem. Eng. (IJCCE), 40(1): 21–34 (2021).
[10] Yin C., Wang Y., Effect of Sulfidation Process on Catalytic Performance over Unsupported Ni-Mo-W Hydrotreating Catalysts, Korean. J. Chem. Eng., 34: 1004–1012 (2017).
[11] Gao Q., Ofosu T.N.K., Ma S.G., Komvokis V.G., Williams C.T., Segawa K., Catalyst Development for Ultra-Deep Hydrodesulfurization (HDS) of Dibenzothiophenes. I: Effects of Ni Promotion in Molybdenum-Based Catalysts, Catal. Today, 164: 538–543 (2011).
[12] Kokayeff P., Zink S., Roxas P., "Hydrotreating in Petroleum Processing", Handbook of Petroleum Processing, pp. 1-59 (2015).
[15] AL-Hammadi S.A., Al-Amer A.M., Saleh T.A., Alumina-Carbon Nanofiber Composite as a Support for MoCo Catalysts in Hydrodesulfurization Reactions, Chem. Eng. J., 345: 242–251 (2018).
[16] Han W., Nie H., Long X., Li M., Yang Q., Li D., Effects of the Support BrØnsted Acidity on the Hydrodesulfurization and Hydrodenitrogention Activity of Sulfided NiMo/Al2O3 Catalysts, Catal. Today, 292: 58–66 (2017).
[18] Kohli K., Prajapati R., Maity S.K., Sharma B.K., Effect of Silica, Activated Carbon, and Alumina Supports on NiMo Catalysts for Residue Upgrading, Energies, 13: 1–16 (2020).
[19] Argyle M.D., Bartholomew C.H., Heterogeneous Catalyst Deactivation and Regeneration: A Review, Catalysts, 5: 145–269 (2015).
[20] Liu M., Zhang L.Z., Zhang C., Yuan S.H., Zhao D.Z., Duan L.H., Transformation of Nitrogen-Containing Compounds in Atmospheric Residue by Hydrotreating, Korean. J. Chem. Eng., 35: 375–382 (2018).
[21] Liakakou E.T, Heracleous E., Triantafyllidis K.S., Lemonidou A.A., K-Promoted NiMo Catalysts Supported on Activated Carbon for the Hydrogenation Reaction of CO to Higher Alcohols: Effect of Support and Active Metal, Appl. Catal. B Environ., 165: 296–305 (2015).
[22] Gu L., Dong G., Yu H., Zhang K., Lu X., Wen H., et al., Preparation of Porous Biochar by Urine Assisted Pyrolysis of Sewage Sludge and their Application for Eriochrome Black T Adsorption, J. Anal. Appl. Pyrolysis, 153:104975 (2020).
[23] Sekirifa M.L., Hadj-Mahammed M., Pallier S., Baameur L., Richard D., Al-Dujaili A.H., Preparation and Characterization of an Activated Carbon from
a Date Stones Variety by Physical Activation with Carbon Dioxide
, J. Anal. Appl. Pyrolysis, 99: 155–160 (2013).
[24] Ahmadpour A, Do DD., The Preparation of Active Carbons from Coal by Chemical and Physical Activation, Carbon N Y, 34: 471–479 (1996).
[25] Maciá-Agulló J.A., Moore B.C., Cazorla-Amorós D., Linares-Solano A., Activation of Coal Tar Pitch Carbon Fibres: Physical Activation vs. Chemical Activation, Carbon N Y, 42: 1367–1370 (2004).
[27] Nath Prajapati Y., Verma N., Hydrodesulfurization of Thiophene on Activated Carbon Fiber Supported NiMo Catalysts, Energy and Fuels, 32: 2183–2196 (2018).
[28] Akcil A., Vegliò F., Ferella F., Demet M., Tuncuk A., A Review of Metal Recovery from Spent Petroleum Catalysts and Ash, Waste Manag, 45: 420–433 (2015).
[29] Abbas M.N., Alalwan H.A., Catalytic Oxidative and Adsorptive Desulfurization of Heavy Naphtha Fraction, Korean Chemical Engineering Research, 57: 1–6 ( 2019).
[30] Sakanishi K., Nagamatsu T., Mochida I., Whitehurst D.D., Hydrodesulfurization Kinetics and Mechanism of 4,6-dimethyldibenzothiophene over NiMo Catalyst Supported on Carbon, J. Mol. Catal. A Chem., 155: 101–109 (2000).
[35] Zhang J., Li X., Chen H., Qi M., Zhang G., Hu H., et al., Hydrogen Production by Catalytic Methane Decomposition: Carbon Materials as Catalysts or Catalyst Supports, Int. J. Hydrogen Energy, 42: 19755–19775 (2017).
[37] Karimnezhad L., Haghighi M., Fatehifar E., Adsorption of Benzene and Toluene from Waste Gas Using Activated Carbon Activated by ZnCl2, Front Environ Sci Eng, 8: 835–844 (2014).
[39] Açıkalın K., Thermogravimetric Analysis of Walnut Shell as Pyrolysis Feedstock, J. Therm. Anal. Calorim., 105: 145–150 (2011).
[40] Uzun B.B., Yaman E., Pyrolysis Kinetics of Walnut Shell and Waste Polyolefins Using Thermogravimetric Analysis, J Energy Inst, 90: 825–837 (2017).
[42] Abubakar U.C., Alhooshani K.R., Adamu S., Al Thagfi J., Saleh T.A., The Effect of Calcination Temperature on the Activity of Hydrodesulfurization Catalysts Supported on Mesoporous Activated Carbon, J. Clean. Prod., 211: 1567–1575 (2019).
[45] Rambabu N., Badoga S., Soni K.K., Dalai A.K., Adjaye J., Hydrotreating of Light Gas Oil Using a NiMo Catalyst Supported on Activated Carbon Produced from Fluid Petroleum Coke, Front. Chem. Sci. Eng., 8: 161–170 (2014).
[46] Abubakar U.C., Alhooshani K.R., Adamu S., Al Thagfi J., Saleh T.A., The Effect of Calcination Temperature on the Activity of Hydrodesulfurization Catalysts Supported on Mesoporous Activated Carbon, J. Clean. Prod., 211: 1567–1575 (2019).
[47] Ding L., Zheng Y., Zhang Z., Ring Z., Chen J., Hydrotreating of Light Cycled Oil Using WNi/Al2O3 Catalysts Containing Zeolite Beta and/or Chemically Treated Zeolite Y., J. Catal., 241: 435-445 (2006).
[48] Mahmoudabadi Z.S., Rashidi A., Tavasoli A., Synthesis of MoS2 Quantum Dots as a Nanocatalyst for Hydrodesulfurization of Naphtha: Experimental and DFT Study, J. Environ. Chem. Eng., 8 (2020).
[49] Mahmoudabadi Z.S., Tavasoli A., Rashidi A., Esrafili M., Catalytic Activity of Synthesized 2D MoS2/Graphene Nanohybrids for the Hydrodesulfurization of SRLGO: Experimental and DFT Study, Environ. Sci. Pollut. Res., 28: 5978–5990 (2021).
[50] Hita I., Palos R., Arandes J.M., Hill J.M., Castaño P., Petcoke-Derived Functionalized Activated Carbon as Support in a Bifunctional Catalyst for Tire Oil Hydroprocessing, Fuel Process Technol., 144: 239–247 (2016).
[51] Román-Martínez M.C., Cazorla-Amorós D., Linares-Solano A., de Lecea C.S.M., TPD and TPR Characterization of Carbonaceous Supports and Pt/C Catalysts, Carbon N Y, 31:895–902 (1993).
[52] Nabgan W., Rashidzadeh M., Nabgan B., The Catalytic Naphtha Reforming Process: Hydrodesulfurization, Catalysts and Zeoforming, Environ. Chem. Lett., 16: 507–522 (2018).
[54] Abid M.F., Ahmed S.M., Abohameed W.H., Ali S.M., Study on Hydrodesulfurization of a Mixture of Middle Distillates, Arab. J. Sci. Eng., 43: 5837–5850 (2018).
[55] Behnejad B., Abdouss M., Tavasoli A., Ni-mo Supported Nanoporous Graphene as a Novel Catalyst for HDS and Hdn of Heavy Naphtha, Brazilian J. Chem. Eng., 36: 265–273 (2019).
[56] Behnejad B., Abdouss M., Tavasoli A., Comparison of Performance of Ni–Mo/γ-alumina Catalyst in HDS and HDN Reactions of Main Distillate Fractions, Pet. Sci, 16: 645–656 (2019).
[57] Behnejad B., Abdouss M., Tavasoli A., Effect of Graphene Functionalizing on the Performance of NiMo/Graphene in HDS and HDN Reactions, Pet. Sci., 16: 1185–1195 (2019).