A response surface methodology (RSM) with 3 levels and 4 variables was used to model and optimize the n-heptane isomerization kinetic process over Pt-HZSM-5/HMS catalysts in a fixed bed micro reactor. 30 sets of isomerization rate tests were performed at different conditions of H2 flow rate (20-45 ccmin−1), n-heptane flow rate (2-4.5 cch−1), the temperatures (200-350 °C), and the weight percent of HZSM-5 (10-40%). It was observed that the amounts of HZSM-5 into Pt-HMS structure has the greatest effect on the rate of reaction. The surface and contour plots confirm that the rates do not considerably change versus temperature, n-heptane and H2 flow rates. 0.24 molg−1s−1 is the highest reaction rate obtained in the 4.5 cch−1 n-heptane and 45 cc min−1 H2 flow rate. The RSM was effective for predicting and optimizing this process. The modelling results also show both power-law and Langmuir–Hinshelwood models are in agreement with the experimental data.
Parsafard, N. (2023). Modelling and optimization: Isomerization reaction rate using response surface methodology with two kinetic model over bi-porous catalysts. Journal of Chemical and Petroleum Engineering, (), -. doi: 10.22059/jchpe.2023.346017.1398
MLA
Nastaran Parsafard. "Modelling and optimization: Isomerization reaction rate using response surface methodology with two kinetic model over bi-porous catalysts". Journal of Chemical and Petroleum Engineering, , , 2023, -. doi: 10.22059/jchpe.2023.346017.1398
HARVARD
Parsafard, N. (2023). 'Modelling and optimization: Isomerization reaction rate using response surface methodology with two kinetic model over bi-porous catalysts', Journal of Chemical and Petroleum Engineering, (), pp. -. doi: 10.22059/jchpe.2023.346017.1398
VANCOUVER
Parsafard, N. Modelling and optimization: Isomerization reaction rate using response surface methodology with two kinetic model over bi-porous catalysts. Journal of Chemical and Petroleum Engineering, 2023; (): -. doi: 10.22059/jchpe.2023.346017.1398