Catalytic Cracking of Oily Sludge using Nickel Metal Catalyst Embedded in Silica Derived from Adsorbent in a Gas Process Plant

  • Novita Jayanti Department of Chemical Engineering, Faculty of Engineering, Universitas Gadjah Mada, Yogyakarta 55281, Indonesia
  • Nazarudin Department of Chemical Engineering, Faculty of Sains and Technology, University of Jambi, Jambi 36361, Indonesia
  • Panut Mulyono Department of Chemical Engineering, Faculty of Engineering, Universitas Gadjah Mada, Yogyakarta 55281, Indonesia
Keywords: Catalytic Cracking, Ni Metal, Oily Sludge, RSM, Silica

Abstract

Abstract. One of the Oily Sludge (OS) recycling methods is through catalytic cracking. This process involves the reaction breaking down large molecules into smaller ones with the help of a catalyst. Nickel (Ni) metal is often used as a catalyst because it can increase fuel liquid yield while reducing the coke formation. To enhance its performance, Ni metal can be embedded in a carrier material like Silica to form the Ni-Silica catalyst. In this research, OS sourced from a Gas Process Plant is treated with catalytic cracking using Ni-Silica, where the Silica used is derived from an Adsorbent activated with NaOH. Optimization of the cracking conditions is carried out using Response Surface Methodology (RSM) with a Box-Behnken design. The optimized cracking reaction conditions include temperature (713 K, 723 K, and 733 K), time (50 min, 60 min, and 70 min), and catalyst-to-OS ratio of 1:5, 1:6, and 1:7. Statistical analysis indicates that the relationship between the reaction condition variables and the Oil Liquid Product (OLP) falls into the moderate category, as shown by the coefficient of determination (R²) of 0.5. The calculated F-value for the deviation from the mathematical model is smaller than the F-Table value (9.2) at both 5% and 1% significance levels, with a value of 0.6. This indicates that the mathematical model generated can be accepted as the mathematical model within the range of reaction conditions in this study. Calculus analysis reveals that the optimum reaction conditions are a temperature of 717.34 K, a time of 58.58 min, and a catalyst-to-OS ratio of 1:6, 15. Canonical analysis indicates that for OLP, λ1= [-12.38], λ2= [-2.27], and λ3= [4.50], where lambda values indicate that the most sensitive response surface parameter for OLP is temperature, followed by the catalyst-to-sample ratio, and the least sensitive is reaction time.

 

Keywords: Catalytic Cracking, Ni Metal, OS, RSM, Silica

References

Alnajjar, M., Hethnawi, A., Nafie, G., Hassan, A., Vitale, G., and Nassar, N.N., 2019. “Silica-alumina composite as an effective adsorbent for the removal of metformin from water.” J. Environ. Chem. Eng. 7, 1–10.

Amin, M.H., 2020. “Relationship between the pore structure of mesoporous Silica supports and the activity of Nickel nanocatalysts in the CO2 reforming of methane.” Catalysts 10, 1–21.

Choi, D.S., Kim, J., Kim, N.Y., and Joo, J.B., 2022. “Control of textural property in spherical alumina ball for enhanced catalytic activity of Ni-supported Al2O3 catalyst in steam–methane reforming.” J. Ind. Eng. Chem. 108, 400–410.

Fakhroleslam, M., and Sadrameli, S.M., 2019. “Thermal/catalytic cracking of hydrocarbons for the production of olefins; a state-of-the-art review III: Process modeling and simulation.” Fuel 252, 553–566.

Gea, S., Haryono, A., Andriayani, A., Sihombing, J.L., Pulungan, A.N., Nasution, T., Rahayu, R., and Hutapea, Y.A., 2020. “The effect of chemical activation using base solution with various concentrations towards sarulla natural zeolite.” Elkawnie 6, 85.

Hochberg, S.Y., Tansel, B., and Laha, S., 2022. “Materials and energy recovery from OSs removed from crude oil storage tanks (tank bottoms): A review of technologies.” J. Environ. Manage. 305, 114428.

Huang, Q., Wang, J., Qiu, K., Pan, Z., Wang, S., Chi, Y., and Yan, J., 2015. “Catalytic pyrolysis of petroleum sludge for production of hydrogen-enriched syngas.” Int. J. Hydrogen Energy 40, 16077–16085.

Ibrahim, S.A., Ekinci, E.K., Karaman, B.P., and Oktar, N., 2021. “Coke-resistance enhancement of mesoporous γ-Al2O3 and MgO-supported Ni-based catalysts for sustainable hydrogen generation via steam reforming of acetic acid.” Int. J. Hydrogen Energy 46, 38281–38298.

Jia, H., Zhao, S., Zhou, X., Qu, C., Fan, D., and Wang, C., 2017. “Low-temperature pyrolysis of OS: Roles of Fe/Al-pillared bentonites.” Arch. Environ. Prot. 43, 82–90.

Jin, X., Teng, D., Fang, J., Liu, Y., Jiang, Z., Song, Y., Zhang, T., Siyal, A.A., Dai, J., Fu, J., Ao, W., Zhou, C., Wang, L., and Li, X., 2021. “Petroleum oil and products recovery from OS: Characterization and analysis of pyrolysis products.” Environ. Res. 202, 111675.

Kasmin, N.H., Zubairi, S.I., Lazim, A.M., and Awang, R., 2020. “Thermal treatments on the oil palm fruits: Response surface optimization and microstructure study.” Sains Malaysiana 49, 2301–2309.

Lee, Y., Shin, J., Kwak, J., Kim, S., Son, C., Cho, K., Chon, K. 2021. "Effects of NaOH activation on adsorptive removal of herbicides by biochar prepared from ground coffe residues: A review." Int. J. Energy Res. 14, 1297.

Li, J., Lin, F., Li, K., Zheng, F., Yan, B., Che, L., Tian, W., Chen, G., and Yoshikawa, K., 2021. “A critical review on energy recovery and non-hazardous disposal of OS from petroleum industry by pyrolysis.” J. Hazard. Mater. 406, 124706.

Lin, B., Wang, J., Huang, Q., Ali, M., and Chi, Y., 2017a. “Aromatic recovery from distillate oil of OS through catalytic pyrolysis over Zn modified HZSM-5 zeolites.” J. Anal. Appl. Pyrolysis 128, 291–303.

Lin, B., Wang, J., Huang, Q., and Chi, Y., 2017b. “Effects of potassium hydroxide on the catalytic pyrolysis of OS for high-quality oil product.” Fuel 200, 124–133.

Liu, C., Hu, X., Xu, Q., Zhang, S., Zhang, P., Guo, H., You, Y., and Liu, Z., 2021. “Response surface methodology for the optimization of the ultrasonic-assisted rhamnolipid treatment of OS.” Arab. J. Chem. 14.

Lu, F., Chen, X., Lei, Z., Wen, L., and Zhang, Y., 2021. “Revealing the activity of different iron carbides for Fischer-Tropsch synthesis.” Appl. Catal. B Environ. 281, 119521.

Murungi, P.I., and Sulaimon, A.A., 2022. “Petroleum sludge treatment and disposal techniques: a review.” Environ. Sci. Pollut. Res. 29, 40358–40372.

Naidu, B.N., Kumar, K.D.P.L., Saini, H., Kumar, M., Kumar, T.N., and Prasad, V.V.D.N., 2022. “Coke deposition over Ni-based catalysts for dry reforming of methane: effects of MgO-Al2O3 support and ceria, lanthana promoters.” J. Environ. Chem. Eng. 10, 106980.

Nazarudin, Jayanti, N., Alfernando, O., Prabasari, I.G., Ulyarti, and Sarip, R., 2020. “Catalytic cracking of polyethylene terephthalate (PET) plastic waste and palm fibre mixtures using Ni-USY zeolite catalyst.” J. Phys. Conf. Ser. 1567.

Okoronkwo, E.A., Imoisili, P.E., Olubayode, S.A., and Olusunle, S.O.O., 2016. “Development of Silica Nanoparticle from Corn Cob Ash.” Adv. Nanoparticles 05, 135–139.

Oyebanji, J.A., Okekunie, P.O., Itabiyi, O.E., 2023. " Box Behnken design application for optimization of bio-oil yield from catalytic pyrolysis of agro-residue." Fuel Communications. 16, 100091.

Saravanan, S and Dubey, R.S. 2020. Romanian Journal. 105 - 112.

Sharma, S.K., Verma, D.S., Khan, L.U., Kumar, S., and Khan, S.B., 2018. “Handbook of Materials Characterization.” Handb. Mater. Charact. 1–613.

Shi, S., 2018. “Advances in modeling hydrocarbon cracking kinetic predictions by quantum chemical theory: A review.” Int. J. Energy Res. 42, 3164–3181.

Tran, T.N., Pham, T.V., Le, M.L., Nguyen, T.P., Tran, V.M. 2013. " Synthesis of amorphous silica and sulfonic acid functionalized silica used as reinforced phase for polymer electrolyte membrane." Adv. Nat. Sci.: Nanosci. Nanotechnol. 4, 045007

Triyono, T., Trisunaryanti, W., Falah, I., Rahmi, L. 2023. "Effect of acetic acid and/or sodium hydroxide treatment towards characters of wonosari natural zeolite for hydrotreatment of castor oil into biofuel." Indones. J. Chem. 23, 298 -308.

Tsiotsias, A.I., Charisiou, N.D., Sebastian, V., Gaber, S., Hinder, S.J., Baker, M.A., Polychronopoulou, K., and Goula, M.A., 2022. “A comparative study of Ni catalysts supported on Al2O3, MgO–CaO–Al2O3 and La2O3–Al2O3 for the dry reforming of ethane.” Int. J. Hydrogen Energy 47, 5337–5353.

Wang, J., Lin, B.C., Huang, Q.X., Ma, Z.Y., Chi, Y., and Yan, J.H., 2017. “Aromatic hydrocarbon production and catalyst regeneration in pyrolysis of OS using ZSM-5 zeolites as catalysts.” Energy and Fuels 31, 11681–11689.

Zhang, X., Xu, J., Ran, S., Gao, Y., Lyu, Y., Pan, Y., Cao, F., Lin, Y., Yang, Z., Wang, Z., Guo, D., Wang, Q., Zhu, L., and Zhu, Y., 2022. “Experimental study on catalytic pyrolysis of OS for H2 production under new nickel-ore-based catalysts.” Energy 249, 123675.

Published
2024-04-30
How to Cite
Jayanti, N., Nazarudin, & Mulyono, P. (2024). Catalytic Cracking of Oily Sludge using Nickel Metal Catalyst Embedded in Silica Derived from Adsorbent in a Gas Process Plant. ASEAN Journal of Chemical Engineering, 24(1), 36-52. https://doi.org/10.22146/ajche.10272
Section
Articles