1. Study on novel scheme for hydrodesulfurization of middle distillates using different types of catalyst
- Author
-
Mohammad F. Abid, Shakir M. Ahmed, Waleed H. AbuHamid, and Salah M. Ali
- Subjects
Engineering (General). Civil engineering (General) ,TA1-2040 - Abstract
This study aimed to investigate the hydrodesulfurization (HDS) of a mixture of crude oil fractions (e.g., naphtha, kerosene, and gas oil) all in one time in a single reactor under various operating parameters such as temperature (T = 310–370 °C), pressure (P = 40–55 bar), weight hour space velocity (WHSV = 1.2–3.6 h−1), hydrogen-to- hydrocarbon ratio (150–300 vol/vol), and type of catalysts (di-metallic and tri-metallic). Experimental results showed that temperature and pressure have positive effects on process performance while weight hour space velocity gives a different trend. Results indicated that HDS efficiency was 95.8% at optimized operating parameters T = 350 °C, P = 50 bars, WHSV = 1.2 h−1, and (H2/HC) ratio = 200 vol/vol. and with NiCoMo/γ-Al2O3 catalyst which offered a higher HDS efficiency compared with other types of catalysts used. Kinetic analysis revealed that a pseudo-first order rate law is well expressing the HDS reaction of the operating system for all types of catalysts. Estimation of rate parameters over each type of catalyst was also presented. Study of mass transfer limitations revealed that surface reaction is the rate controlling step. Feasibility of the proposed technique may offer a large reduction in fixed and operating costs of the HDS unit in a modern petroleum refinery. Keywords: Hydrotreatment, Crude oil fractions, Sulfur removal, Catalytic reactor, Kinetic analysis, Di-metallic catalyst, Tri-metallic catalyst
- Published
- 2019
- Full Text
- View/download PDF