Analysis of the co-hydrogenation process of coal tar and kitchen waste oil based on reaction kinetics model

Kitchen waste oil (KWO) and coal tar (CT) are two commonly used alternatives to crude oil for fuel production through hydrogenation. If these two raw materials can be co-hydrogenated, it will help broaden the company's sources of raw materials. Therefore, in order to reveal the positive and negative impacts of the co-hydrogenation process of these two materials and to conduct a quantitative analysis of these phenomena, co-hydrogenation experiments of CT and KWO were completed in this study. The reaction kinetics parameters of the co-hydrogenation reaction were calculated. Experiments have shown that co-hydrogenation with coal tar hydrogenation products (CTHP) can increase the hydrogenation efficiency of KWO by approximately 1.5 %. This promoting effect is mainly attributed to the hydrogen-supplying properties of compounds such as tetralin and hexahydro naphthalene present in the CTHP. Through a combined model of reaction kinetics and thermodynamics, it is calculated that the activation energy of KWO hydrodeoxygenation under the action of catalysts is 50.936 kJ·mol−1, while under the action of CTHP hydrogen supply, it is 148.429 kJ·mol−1, and this promoting effect accounts for 19.3 % of the total reaction (as deduced from comparing reaction rate constants). The experimental data presented in this paper and the calculated reaction parameters can provide a basis for design improvements in technology. •Co-hydrogenation with coal tar enhances kitchen waste oil hydrodeoxygenation.•Co-hydrogenation with coal tar improves kitchen waste oil hydrogenation by 1.5 %.•The Ea for kitchen waste oil hydrodeoxygenation with coal tar is 148.4 kJ/mol.•The promoting effect of coal tar accounts for 19.3 % of the total reaction.