Direct sulfonation of methane with SO 3 to methanesulfonic acid (MSA) is accomplished in sulfuric acid with almost 100% selectivity in the presence of a catalyst, namely, Ce and Rh salts and molecular oxygen as the catalyst regenerator. In the absence of O 2 , the catalyst remains effective but the selectivity to MSA decreases to 53% and byproducts, principally CH 3 OSO 3 H, are formed. The effects of O 2 pressure, catalyst concentration, temperature, SO 3 concentration, and methane pressure have been examined on the rate of SO 3 conversion to MSA. The conversion of SO 3 to MSA was the same when CF 3 SO 3 H was used as the solvent instead of H 2 SO 4 .Keywords: C À H activation; metal catalyst; methane; methanesulfonic acid; molecular oxygen; sulfonation; sulfur trioxide Methanesulfonic acid (MSA, 70 wt %) is widely used in electrochemical systems and is an excellent catalyst for the esterification, alkylation, and condensation of organic compounds. [1] Lower reaction temperatures are required when using MSA rather than titanate catalysts, and purer, more colorless products can be obtained using MSA than those produced using sulfuric or para-toluenesulfonic acid as the catalyst. Anhydrous MSA is also particularly well suited for pharmaceutical applications and as a catalyst for aromatic alkylation. The current commercial process for the synthesis of MSA involves chlorine oxidation of methylmercaptan. [2] While this process is highly productive, it produces six moles of HCl per mole of MSA, resulting in a coupling of the demand for the primary product and the byproduct. As an alternative it is interesting to consider a direct methane sulfonation route using SO 3 or SO 2 and O 2 as the sulfonating agent. Sen and co-workers [3a] and, more recently, we [3b, c] have shown that a compound such as K 2 S 2 O 8 can be used as a free radical initiator [3d] to sulfonate methane with SO 3 in fuming sulfuric acid.Identification of a catalytic process for the sulfonation of methane would highly desirable, since this would eliminate the need for a free-radical initiator. While Ishii and co-workers have reported success in the vanadium-catalyzed sulfonation of adamantane to the corresponding sulfonic acids using SO 2 and O 2 , methane did not undergo sulfonation to MSA. [4] Hg-based catalysts have been used at elevated temperature (300 ± 450 8C) for methane sulfonation with SO 3 to MSA; however this process exhibits a low yield and cannot be implemented due to problems in isolating MSA from a mixture of byproducts, mainly esters and disulfonic acids formed during this reaction. [5] In subsequent studies, Periana and co-workers [6] have reported the selective sulfonation of CH 4 to MSA in fuming sulfuric acid at 180 to 220 8C using Hg salts [6a] or Pt complexes as the catalyst. [6b] In both the cases, the metal cations undergo reduction and are reoxidized by sulfuric acid. [6] We have recently shown that Hg(CF 3 SO 3 H) 2 can be used in the presence of O 2 to synthesize MSA by the reaction of methane and SO 3 in ...