cis‐Pinane, the hydrogenation product of pinene, is a key chemical intermediate and its production is an important forest chemical process. In this study, α‐pinene was hydrogenated using a nickel‐supported aluminophosphate catalyst (Ni/APO‐PT) in the batch mode of operation. The pore structure of the catalyst was characterized, the process parameters were studied, the hydrogenation process was optimized, and the kinetic study was conducted. The results showed that the conversion of pinene was positively correlated with temperature, duration, and catalyst dosage. In contrast, the selectivity of cis‐pinane was negatively correlated with temperature and catalyst dosage. An optimization was performed using the response surface methodology (RSM). A selectivity of 96.2% was obtained with α‐pinene conversion of 98.5% under optimal conditions, that is, a temperature of 405 K, reaction time of 60 min, hydrogen pressure of 3 MPa, and catalyst loading of 3.32 wt%. The reusability of the catalyst was studied, and the catalyst was found to maintain efficient activity for seven cycles. The kinetics of hydrogenation were investigated using both linear and nonlinear methods in the absence of diffusional limitation. In the temperature range from 403 to 433 K, the hydrogenation of α‐pinene to pinane was compatible with the pseudo‐first‐order process, and the activation energies for the formation of cis‐pinane and trans‐pinane were 41.8 and 56.1 kJ/mol, respectively. This study shows that the performance of the Ni/APO‐PT catalyst is similar to that of noble metals and the catalyst has the potential for industrial applications.