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Hydrometallurgical Recovery of Valuable Metals from Hazardous Petrochemical Industry Waste and Kinetic Investigation

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Abstract

A significant amount of spent Ni-Mo HDS catalyst hazardous waste is generated during the petroleum refining processes. This waste contains valuable metals such as Mo, Ni, and Al. The most interesting route for a sustainable waste management is the recovery of valuable metals from the environmental and economic point of view. In this work, hydrometallurgical method was used to investigate the recovery of valuable metals from roasted Ni-Mo HDS catalyst and determine the effect of particle size, stirring speed, acid concentration, and temperature on the leaching rate of MoO3, NiMoO4, Al2O3, and AlPO4. Optimum leaching conditions, in which 92% of MoO3, 93% of NiMoO4, 55% of Al2O3, and 71% of AlPO4 leached, were determined as 180 min of reaction time, unground catalyst, stirring speed of 300 min−1, 2 M HCl solution, and 328 K. Avrami Kinetic Model was found to be the most suitable kinetic model for the experimental data obtained from the leaching experiments. Kinetic parameters used in Avrami Kinetic Model were calculated for the leaching reactions of MoO3, NiMoO4, Al2O3, and AlPO4. Apparent activation energy values were calculated for the leaching reaction of MoO3, NiMoO4, Al2O3, and AlPO4 in HCl solutions as 31.43, 45.42, 42.37, and 51.07 kJ mol−1, respectively. Experimental results and kinetic calculations showed that leaching rates of NiMoO4, Al2O3, and AlPO4 are more temperature dependent than that of MoO3 due to having higher apparent activation energy values. Model kinetic equation, which gives fraction of compound extracted values as a function of time, was derived as \(\text{X} = \text{1-exp}{\left[-{\text{A}}_{\text{o}}{{\text{C}}}_{\text{o}}^{\text{m}}{\text{exp}}\left({- }\frac{\text{E}}{\text{R T}}\right){\text{t}}\right]}^{\text{n}}\).

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References

  1. Akcil A et al (2015) A review of metal recovery from spent petroleum catalysts and ash. Waste Manage 45:420–433

    CAS  Google Scholar 

  2. Zeng L, Cheng CY (2009) A literature review of the recovery of molybdenum and vanadium from spent hydrodesulphurisation catalysts: part I: metallurgical processes. Hydrometallurgy 98(1):1–9

    CAS  Google Scholar 

  3. Ahmed HS, Menoufy MF (2012) New trends in hydroprocessing spent catalysts utilization. In: Petrochemicals, p 249–258

  4. Yang C, Wu J, Wang W, Li B, Zhang B, Ding Y (2018) Sustainable management of spent hydroprocessing catalyst. Trends Renew Energy 4(1):90–95

    Google Scholar 

  5. Nguyen TH, Lee MS (2014) Recovery of molybdenum and vanadium with high purity from sulfuric acid leach solution of spent hydrodesulfurization catalysts by ion exchange. Hydrometallurgy 147–148:142–147

    Google Scholar 

  6. Valverde IM, Paulino JF, Afonso JC (2008) Hydrometallurgical route to recover molybdenum, nickel, cobalt and aluminum from spent hydrotreating catalysts in sulphuric acid medium. J Hazard Mater 160(2):310–317

    CAS  Google Scholar 

  7. Ilhan S, Akgün D (2021) Leaching Kinetics of Mo, Ni, and Al oxides from spent nickel-molybdenum hydrodesulfurization catalyst in H2SO4 solution. J Sustain Metall 7(2):470–480

    Google Scholar 

  8. Mulak W, Miazga B, Szymczycha A (2005) Kinetics of nickel leaching from spent catalyst in sulphuric acid solution. Int J Miner Process 77(4):231–235

    CAS  Google Scholar 

  9. Nazemi MK, Rashchi F, Mostoufi N (2011) A new approach for identifying the rate controlling step applied to the leaching of nickel from spent catalyst. Int J Miner Process 100(1):21–26

    CAS  Google Scholar 

  10. Lim MSW et al (2021) Intensification and optimisation of nickel recovery from spent hydrogenation catalysts via ultrasound-augmented hydrometallurgy. J Environ Chem Eng 9(4):105771

    CAS  Google Scholar 

  11. Chen R et al (2022) Stepwise separation and recovery of molybdenum, vanadium, and nickel from spent hydrogenation catalyst. Hydrometallurgy 213:105910

    CAS  Google Scholar 

  12. Sheik AR et al (2013) Dissolution kinetics of nickel from spent catalyst in nitric acid medium. J Taiwan Inst Chem Eng 44(1):34–39

    CAS  Google Scholar 

  13. Banda R et al (2013) Recovery of valuable metals and regeneration of acid from the leaching solution of spent HDS catalysts by solvent extraction. Hydrometallurgy 133:161–167

    CAS  Google Scholar 

  14. Parhi PK, Park KH, Senanayake G (2013) A kinetic study on hydrochloric acid leaching of nickel from Ni–Al2O3 spent catalyst. J Ind Eng Chem 19(2):589–594

    CAS  Google Scholar 

  15. Rabah MA, Hewaidy IF, Farghaly FE (1997) Recovery of molybdenum and cobalt powders from spent hydrogenation catalyst. Powder Metall 40(4):283–288

    CAS  Google Scholar 

  16. Lai Y-C et al (2008) Metal recovery from spent hydrodesulfurization catalysts using a combined acid-leaching and electrolysis process. J Hazard Mater 154(1):588–594

    CAS  Google Scholar 

  17. de Lima TS, Campos PC, Afonso JC (2005) Metals recovery from spent hydrotreatment catalysts in a fluoride-bearing medium. Hydrometallurgy 80(3):211–219

    Google Scholar 

  18. Rezki, A.S., et al. Molybdenum Extraction from Spent Catalyst Using Citric Acid: Characteristic and Kinetics Study. In IOP Conference Series: Earth and Environmental Science. 2021. IOP Publishing.

  19. Marafi M et al (1989) Regeneration of spent hydroprocessing catalysts: metals removal. Appl Catal 47(1):85–96

    CAS  Google Scholar 

  20. Ilhan S (2020) Extraction of molybdenum, nickel and aluminium from spent Ni–Mo hydrodesulphurization (HDS) catalyst in oxalic acid solutions. Can Metall Q 59(1):26–35

    CAS  Google Scholar 

  21. Zoraga M (2023) Metal recovery from spent Ni-Mo-V hydrodesulphurisation catalyst in oxalic acid media by mechanochemical treatment. Can Metall Quarterly. https://doi.org/10.1080/00084433.2023.2221579

    Article  Google Scholar 

  22. Erust C et al (2016) Recovery of vanadium from spent catalysts of sulfuric acid plant by using inorganic and organic acids: laboratory and semi-pilot tests. Waste Manage 49:455–461

    CAS  Google Scholar 

  23. Mulak W et al (2006) Preliminary results of metals leaching from a spent hydrodesulphurization (HDS) catalyst. Physicochem Prob Min Process 40:69–76

    CAS  Google Scholar 

  24. Szymczycha-Madeja A (2011) Kinetics of Mo, Ni, V and Al leaching from a spent hydrodesulphurization catalyst in a solution containing oxalic acid and hydrogen peroxide. J Hazard Mater 186(2):2157–2161

    CAS  Google Scholar 

  25. Huang S et al (2014) Alkali extraction of valuable metals from spent Mo–Ni/Al2O3 catalyst. Int J Refract Metal Hard Mater 46:109–116

    CAS  Google Scholar 

  26. Chen Y et al (2006) Investigations on the extraction of molybdenum and vanadium from ammonia leaching residue of spent catalyst. Int J Miner Process 79(1):42–48

    CAS  Google Scholar 

  27. Arslanoğlu H (2021) Selective recovery of molybdenum from petroleum industry waste spent HydrodesulfurizationMo–Co–Ni/Al2O3 catalystin the presence of ammonia: process optimization and kinetic studies. Pet Chem 61(2):198–205

    Google Scholar 

  28. Villarreal MS et al (1999) Recovery of vanadium and molybdenum from spent petroleum catalyst of PEMEX. Ind Eng Chem Res 38(12):4624–4628

    CAS  Google Scholar 

  29. Pinto ISS, Soares HMVM (2012) Selective leaching of molybdenum from spent hydrodesulphurisation catalysts using ultrasound and microwave methods. Hydrometallurgy 129–130:19–25

    Google Scholar 

  30. Wang J et al (2021) Recovering valuable metals from spent hydrodesulfurization catalyst via blank roasting and alkaline leaching. J Hazard Mater 416:125849

    CAS  Google Scholar 

  31. Chen B et al (2023) Recovering valuable metals from spent hydrodesulfurization catalysts by co-leaching, dissociation, and stepwise precipitation. J Environ Chem Eng 11(2):109365

    CAS  Google Scholar 

  32. Arslanoğlu H, Yaraş A (2021) Recovery of molybdenum, cobalt and nickel from spent hydrodesulphurization catalyst through oxidizing roast followed by sodium persulfate leaching. Sustain Mater Technol 28:e00286

    Google Scholar 

  33. Tang H et al (2021) Recovery of platinum-group metals from spent catalysts by microwave smelting. J Clean Prod 318:128266

    CAS  Google Scholar 

  34. Pak JJ, Kim DH, Paek MK, Kim YD (2019) Ferroalloy production from spent petroleum catalysts by reductive smelting and selective oxidation processes. In: Gaustad G, Fleuriault C, Gökelma M, Howarter JA, Kirchain R, Ma K, Meskers C, Neelameggham NR, Olivetti E, Powell AC, Tesfaye F, Verhulst D, Zhang M (eds) REWAS 2019: manufacturing the circular materials economy. Springer, Cham

    Google Scholar 

  35. Howard R, Barnes WJUP (1991) Smelting process for recovery of valuable metals from spent catalysts on an oxide support. US Pat. (5013533)

  36. Medvedev AS, Malochkina NV (2007) Sublimation of molybdenum trioxide from exhausted catalysts employed for the purification of oil products. Russian J Non-Ferrous Metals 48(2):114–117

    Google Scholar 

  37. Gaballah I et al (1994) Valuable metals recovery from spent catalysts by selective chlorination. Resour Conserv Recycl 10(1):87–96

    Google Scholar 

  38. Yang QZ et al (2011) Sustainable recovery of nickel from spent hydrogenation catalyst: economics, emissions and wastes assessment. J Clean Prod 19(4):365–375

    CAS  Google Scholar 

  39. Liang X et al (2022) A review of metallurgical processes and purification techniques for recovering Mo, V, Ni Co, Al from spent catalysts. J Clean Prod 376:134108

    CAS  Google Scholar 

  40. Huang J et al (2010) Concentration and separation of vanadium from alkaline media by strong alkaline anion-exchange resin 717. Rare Met 29(5):439–443

    CAS  Google Scholar 

  41. Padh B et al (2019) Recovery of nickel and molybdate from ammoniacal leach liquors of spent HDS catalysts using chelating ion exchange resin. Hydrometallurgy 184:88–94

    CAS  Google Scholar 

  42. Ghadai B et al (2020) Process development for the recovery of high grade calcium tungstate from alkaline leach liquor of spent HDS catalyst. Hydrometallurgy 191:105237

    CAS  Google Scholar 

  43. Batti NR, Mandre NR (2022) Nickel and aluminium recovery from spent reforming catalyst through selective leaching, crystallization and precipitation. Trans Nonferrous Metals Soc China 32(1):345–353

    CAS  Google Scholar 

  44. Nayak AK, Devi N, Sarangi K (2021) Use of Cyanex 572 as an effective extractant for the recovery of Mo(VI) and V(V) from HDS spent catalyst leach liquor. Sep Purif Technol 275:118960

    CAS  Google Scholar 

  45. Wu H et al (2021) Recovery of nickel and molybdate from ammoniacal leach liquor of spent hydrodesulfurization catalyst using LIX84 extraction. Sep Purif Technol 269:118750

    CAS  Google Scholar 

  46. Cai Y et al (2022) Comprehensive recovery of metals in spent Ni–Mo/γ–Al2O3 hydrofining catalyst. Hydrometallurgy 208:105800

    CAS  Google Scholar 

  47. Han Y et al (2023) A leaching, solvent extraction, stripping, precipitation and calcination process for the recovery of MoO3 and NiO from spent hydrofining catalysts. Hydrometallurgy 218:106046

    CAS  Google Scholar 

  48. Teng Q, Yang Z-C, Wang H-J (2023) Recovery of vanadium and nickel from spent-residue oil hydrotreating catalyst by direct acid leaching-solvent extraction. Trans Nonferrous Metals Soc China 33(1):325–336

    CAS  Google Scholar 

  49. Ilhan S et al (2013) The use of oxalic acid as a chelating agent in the dissolution reaction of calcium molybdate. Metall Mater Trans B 44(3):495–505

    CAS  Google Scholar 

  50. Akimov AS, Sviridenko NN (2022) Transformation of asphaltenes of vacuum residues in thermal and thermocatalytic processes. Pet Sci Technol 40(8):980–994

    CAS  Google Scholar 

  51. Kumar N et al (2019) Dry reforming of methane with isotopic gas mixture over Ni-based pyrochlore catalyst. Int J Hydrogen Energy 44(8):4167–4176

    CAS  Google Scholar 

  52. Berrebi G, Dufresne P, Jacquier Y (1993) Recycling of spent hydroprocessing catalysts: EURECAT technology. Environ Prog 12(2):97–100

    CAS  Google Scholar 

  53. Habashi F (2017) Hydrochloric acid in hydrometallurgy. In: Proceedings of the 56th annual conference of metallurgists, hosting world gold and nickel cobalt. British Columbia, Canada

  54. McKinley C, Ghahreman A (2018) Hydrochloric acid regeneration in hydrometallurgical processes: a review. Min Process Extractive Metall 127(3):157–168

    CAS  Google Scholar 

  55. Faraji F et al (2022) Kinetics of leaching: a review. Rev Chem Eng 38(2):113–148

    CAS  Google Scholar 

  56. Sohn HY (2019) Review of fluid-solid reaction analysis—Part 1: single nonporous reactant solid. Canad J Chem Eng 97(7):2061–2067

    CAS  Google Scholar 

  57. Sohn HY (2019) Review of fluid-solid reaction analysis—Part 2: single porous reactant solid. Canad J Chem Eng 97(7):2068–2076

    CAS  Google Scholar 

  58. Zoraga M, Ilhan S, Kalpakli AO (2020) Leaching kinetics of electric arc furnace dust in nitric acid solutions. Int J Chem Kinet 52(12):933–942

    CAS  Google Scholar 

  59. Li L et al (2017) Sustainable recovery of cathode materials from spent lithium-ion batteries using lactic acid leaching system. ACS Sustain Chem Eng 5(6):5224–5233

    CAS  Google Scholar 

  60. Meng F et al (2020) Selective recovery of valuable metals from industrial waste lithium-ion batteries using citric acid under reductive conditions: Leaching optimization and kinetic analysis. Hydrometallurgy 191:105160

    CAS  Google Scholar 

  61. Fan E et al (2020) Glucose oxidase-based biocatalytic acid-leaching process for recovering valuable metals from spent lithium-ion batteries. Waste Manage 114:166–173

    CAS  Google Scholar 

  62. Wang J et al (2022) Effective separation and recovery of valuable metals from waste Ni-based batteries: a comprehensive review. Chem Eng J 439:135767

    CAS  Google Scholar 

  63. Levenspiel O (1998) Chemical reaction engineering. Wiley, Hoboken

    Google Scholar 

  64. Li Q, Liu Z, Liu Q (2014) Kinetics of vanadium leaching from a spent industrial V2O5/TiO2 catalyst by sulfuric acid. Ind Eng Chem Res 53(8):2956–2962

    CAS  Google Scholar 

  65. Niederkorn JS (1985) Kinetic study on catalytic leaching of sphalerite. JOM 37(7):53–56

    CAS  Google Scholar 

  66. Abdel-Aal EA, Rashad MM (2004) Kinetic study on the leaching of spent nickel oxide catalyst with sulfuric acid. Hydrometallurgy 74(3):189–194

    CAS  Google Scholar 

  67. Sahu KK, Agarwal A, Pandey BD (2005) Nickel recovery from spent nickel catalyst. Waste Manag Res 23(2):148–154

    CAS  Google Scholar 

  68. Habashi F (1969) Principles of Extractive Metallurgy. Gordon and Breach, NY-London-Paris

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Acknowledgements

This work was supported by the Scientific Research Projects Coordination Unit of Istanbul University-Cerrahpasa (Project number: FYL-2021-35642).

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Scientific Research Projects Coordination Unit of Istanbul University-Cerrahpasa, FYL-2021-35642, Sedat İlhan

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Aslan, B.G., Aslan, C. & Ilhan, S. Hydrometallurgical Recovery of Valuable Metals from Hazardous Petrochemical Industry Waste and Kinetic Investigation. J. Sustain. Metall. 9, 1535–1549 (2023). https://doi.org/10.1007/s40831-023-00745-7

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