With the forecasted depletion in global oil reserves, new routes to petrochemical products from natural gas, coal, or biomass are becoming increasingly important. The methanolto-hydrocarbons (MTH) reaction constitutes the final step in one such route. The MTH reaction proceeds over Brønstedacidic zeolite or zeotype catalysts, and near-commercial processes exist for the methanol-to-gasoline (MTG) reaction over ZSM-5, as well as the methanol-to-olefin (MTO) reaction over A breakthrough in the mechanistic understanding of the MTH reaction was the formulation of the "hydrocarbon pool mechanism" by Dahl and Kolboe, [2,3] which postulates that methanol is continuously added to aromatic reaction centers, from which light alkenes are split off in later reaction steps. [4] Recently, the importance of methylation and cracking of alkenes over ZSM-5 was highlighted. [5,6] ZSM-22 (TON) is less well studied [7-10] as a MTH catalyst. It incorporates one-dimensional non-interacting 10-ring channels with diameters of 0.46 0.57 nm. [11] Song and co-workers [7][8][9] reported the failure of ZSM-22 to convert methanol into olefins. Their studies of ZSM-22 showed a low production of olefins during the first pulses of methanol, however the amount of olefin quickly decreased to essentially zero. This failure as an MTH catalyst was ascribed to the narrow pores, which were assumed to be too small to accommodate the complete catalytic cycle of the hydrocarbon pool mechanism. Flow experiments (at 250-400 8C) afforded relatively constant yields of trace amounts of ethene and propene. The low reactivity was believed to be the result of traces of ZSM-11, impurities in the methanol (acetone) and/or external acid sites. Herein, we report studies of the MTH reaction over ZSM-22 at a wider range of reaction conditions and demonstrate that the previous conclusions [7][8][9][10] are not universally valid. Under suitable conditions, ZSM-22 has a conversion capacity comparable to that of SAPO-34, reaction intermediates reside within the pores, and the product spectrum is intermediate to those found for reactions for the MTO and MTG processes.Several batches of ZSM-22 with different Si/Al ratios were synthesized and all were found to be active catalysts for the MTH reaction. The crystallinity and purity of the product were confirmed by X-ray diffraction. Scanning electron microscopy (SEM) revealed needle shaped crystals of 2-3 mm length. 27 Al NMR spectroscopy indicated that, for the samples discussed here, Al was located exclusively in the framework, both for as-made and calcined/ion-exchanged samples. BET surface areas were in the range 160-207 m 2 g À1 . Two different ZSM-22 catalysts (Si/Al = 30 by inductively coupled plasma atomic emission spectroscopy) with BET surface areas of 173 and 207 m 2 g (weight hourly space velocity (WHSV) = 2.05 h À1 ) was 100 % and appreciable conversion took place for several hours (Figure 1 a) . However, at 350 8C, deactivation was very rapid. The feed rate in this case was lower than that used in previous studies...