Siberian Federal University

The new supported zeolite-containing catalyst has been investigated in the reaction of interaction between carbon dioxide and real associated petroleum gases (APG) in presence of water steam at varying experiment temperature within a range of 300-900 °C and space velocity from 1000 to 6000 hr-1. It has been shown that the catalyst performs the high activity in reforming of APG. At 800 °C, the complete conversion of C₂₊ hydrocarbon fraction is occurred, degree of methane conversion gets 92.2 and carbon dioxide conversion - 93.4 %.The main product of reaction is synthesis-gas (mix of carbon oxide and hydrogen) with a ratio of H₂/CO=1.4 at 800 °C. Also water and traces of oxygenates (basically acetic acid) are produced at T ≤ 600 °C. The catalyst works with practically the same activity at increasing space velocity by 4 times. The advantages of the synthesized catalyst are its activity, selectivity, stability, ability to work in water presence, and resistance to coke formation.