Feed Flexibility of CH4 Combined Reforming for Methanol Production

Abstract

Abstract Natural gas with high CO 2 content is a readily available resource, whose application for synthesis gas (syngas) production through dry reforming is strictly limited to processes that require low H 2 /CO ratios. In a recent work we have demonstrated that methanol production through a process scheme based on combined reforming of methane (with CO 2 + H 2 O) becomes a viable alternative from both technical and economic viewpoints. The use of a H 2 separation membrane, as well as a partial H 2 reinjection into the loop reactor, has been considered for the syngas composition adjustment to stoichiometric conditions (M ≈ 2). The reformer and the methanol synthesis reactor were assumed to be working at thermodynamic equilibrium conditions, i.e. at 950 °C and 20 bar for the former, and at 250 °C and 71 bar for the latter. By using a natural gas feed containing 30 % CO 2 and H 2 O/CH 4 = 2, it is feasible to operate the synthesis reactor with a lower recycle ratio, as well as a CO 2 concentration close to the one employed in industrial practice. Under the operating conditions mentioned above, the use of combined reforming for methanol synthesis turns out to be economically advantageous over the classical steam reforming process. In this work a study of the feed flexibility for combined reforming is carried out taking into account the existence of gas fields with CO 2 contents higher than 30 %. Feed mixtures containing 35 % and 40 % CO 2 were analyzed, while maintaining the operating conditions for the reformer (P, T, H 2 O/CH 4 ) and the synthesis reactor (P, T, M). For comparative purposes, a methanol plant producing 400,000 mtpy was considered. A higher CO 2 content in the feed does not significantly alter the CH 4 conversion, but increases the CO 2 conversion and lowers the H 2 /CO ratio. Consequently, it is necessary to increase the separation and reinjection of H 2 to keep stoichiometric conditions in the synthesis reactor. However, a moderate increase in CO 2 concentration in the synthesis reactor cannot be avoided. It is also shown that the recycle ratio should be markedly reduced in order to achieve stable operation. This situation reduces the operating cost of the recycle compressor. On the other hand, the flow of CH 4 + CO 2 to the reformer should be increased for a constant methanol production, which in turn affects the reformer’s energy balance. The main operating costs of the methanol plant, with respect to the reference case (CO 2 /CH 4 = 0.43), grow for CO 2 /CH 4 = 0.55 and CO 2 /CH 4 = 0.67 by 9.5 % and 25 %, respectively. This preliminary technical and economic analysis shows that combined reforming of natural gas with CO 2 content up to 40 % is a feasible process to produce methanol without CO 2 removal.