75-75-2Relevant articles and documents
A high-yield approach to the sulfonation of methane to methanesulfonic acid initiated by H2O2 and a metal chloride
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 2990 - 2993 (2003)
Low temperatures and low pressures suffice for the sulfonation of methane with a suitable free-radical initiator and promoter [Eq. (1)]. Since the RhCl3 promoter can be recycled, and the initiator complex is stable and easy to handle, development of this reaction into an industrial process is promising. MSA = methanesulfonic acid.
Direct catalytic sulfonation of methane with SO2 to methanesulfonic acid (MSA) in the presence of molecular O2
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 1590 - 1591 (2003)
Methane is transformed selectively to methanesulfonic acid at low temperature by liquid-phase sulfonation of methane with SO2 and O2 in the presence of Pd- and Cu-salts as the catalysts.
A novel method for the direct sulfonation of CH4 with SO 3 in the presence of KO2 and a promoter
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 754 - 757 (2003)
Direct sulfonation of methane with SO3 to methanesulfonic acid (MSA) is accomplished in sulfuric acid in the presence of a small amount of KO2 as the free radical initiator and a metal chloride. Of the several metal chlorides examined, RhCl3 was found to be the most effective promoter. While KO2 alone can activate methane, the conversion of SO3 to MSA increases 2.3-fold when KO2 and RhCl3 are both present in the reaction mixture. The effects of different process parameters such as temperature, SO3 concentration, methane pressure, KO2 concentration, and RhCl3 concentration have been examined on the rate of reaction. The reaction is optimized at a KO2-to-RhCl3 molar ratio of 3.16. Strongly acidic solvents such as H2SO4 or CF3SO 3H are necessary for the reaction. No MSA was formed when the reaction was carried out in DMSO. A mechanism is proposed to explain the activation of CH4 to form MSA. A critical part of the sequence is in situ formation of a metal-peroxo species via the reaction of KO2, acid solvent, and RhCl3.
Direct liquid-phase sulfonation of methane to methanesulfonic acid by SO3 in the presence of a metal peroxide
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 1019 - 1021 (2003)
Activation of methane by metal peroxides: Calcium peroxide serves as an effective radical initiator in the liquid-phase sulfonation of methane to methansulfonic acid (MSA) by SO3 [Eq. (1)]. Under the best reaction conditions a 91% conversion of SO3 to MSA was achieved.
Activation of methane to CH3 +: A selective industrial route to methanesulfonic acid
Díaz-Urrutia, Christian,Ott, Timo
, p. 1326 - 1329 (2019)
Direct methane functionalization to value-added products remains a challenge because of the propensity for overoxidation in many reaction environments. Sulfonation has emerged as an attractive approach for achieving the necessary selectivity. Here, we report a practical process for the production of methanesulfonic acid (MSA) from only two reactants: methane and sulfur trioxide. We have achieved >99% selectivity and yield of MSA. The electrophilic initiator based on a sulfonyl peroxide derivative is protonated under superacidic conditions, producing a highly electrophilic oxygen atom capable of activating a C–H bond of methane. Mechanistic studies support the formation of CH3 + as a key intermediate. This method is readily scalable with reactors connected in series for prospective production of up to 20 metric tons per year of MSA.
AgII-Mediated Electrocatalytic Ambient CH4 Functionalization Inspired by HSAB Theory
Deng, Jiao,Guan, Xun,I?iguez, Jesus A.,Liu, Chong,Martinez, Antonio,Xiang, Danlei
, p. 18152 - 18161 (2021)
Although most class (b) transition metals have been studied in regard to CH4 activation, divalent silver (AgII), possibly owing to its reactive nature, is the only class (b) high-valent transition metal center that is not yet reported to exhibit reactivities towards CH4 activation. We now report that electrochemically generated AgII metalloradical readily functionalizes CH4 into methyl bisulfate (CH3OSO3H) at ambient conditions in 98 % H2SO4. Mechanistic investigation experimentally unveils a low activation energy of 13.1 kcal mol?1, a high pseudo-first-order rate constant of CH4 activation up to 2.8×103 h?1 at room temperature and a CH4 pressure of 85 psi, and two competing reaction pathways preferable towards CH4 activation over solvent oxidation. Reaction kinetic data suggest a Faradaic efficiency exceeding 99 % beyond 180 psi CH4 at room temperature for potential chemical production from widely distributed natural gas resources with minimal infrastructure reliance.
Direct sulfonation of methane to methanesulfonic acid by sulfur trioxide catalyzed by cerium(IV) sulfate in the presence of molecular oxygen
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 913 - 916 (2004)
Direct sulfonation of methane with SO3 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 O2, the catalyst remains effective but the selectivity to MSA decreases to 53% and byproducts, principally CH3OSO3H, are formed. The effects of O 2 pressure, catalyst concentration, temperature, SO3 concentration, and methane pressure have been examined on the rate of SO 3 conversion to MSA. The conversion of SO3 to MSA was the same when CF3SO3H was used as the solvent instead of H2SO4.
Direct sulfonation of methane to methanesulfonic acid with SO2 using Ca salts as promoters
Mukhopadhyay, Sudip,Bell, Alexis T.
, p. 4406 - 4407 (2003)
Direct liquid-phase sulfonation of methane to methanesulfonic acid (MSA) with SO2 has been achieved in triflic acid using K2S2O8 as the oxidant and a small amount of a Ca salt as the promoter. The effects of reaction conditions on the conversion of SO2 to MSA were examined. Included were the influence of solvent acidity, reaction duration, reaction temperature, amount of K2S2O8, and composition and amount of promoters. Copyright
PROCESS FOR MANUFACTURING ALKANESULFONIC ACIDS
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Page/Page column 16-18, (2021/04/10)
The present invention relates to an improved process for manufacturing of alkanesulfonic acids.
PROCESS FOR THE PRODUCTION OF ALKANESULFONIC ACIDS
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Page/Page column 7-8, (2021/02/12)
A process for the manufacturing of alkanesulfonic acid by reaction of an alkane with an anhydride in the presence of sulfuric acid and a starter at ambient temperature or higher and under pressure.