2001
DOI: 10.1002/jctb.425.abs
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Production of p‐toluenesulfonic acid by sulfonating toluene with gaseous sulfur trioxide

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Cited by 3 publications
(3 citation statements)
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“…20 It is used in a very broad range of applications, e.g., as a catalyst, detergent solubilizer, resin hardener, in pharmaceuticals, or as an intermediate in the production of saccharine. 21,22 In the literature, different ptsa-based DESs have already been reported but barely characterized, e.g., ptsa:choline chloride at a molar ratio of 1:1, ptsa:benzyltrimethylammonium chloride at a molar ratio of 2.3:1, ptsa:allyltriphenylphosphonium bromide at a molar ratio 3:1, or ptsa:n,n-diethylenethanol ammonium chloride. 23−31 In this paper, combinations of ptsa with different HBAs were prepared in a 1:1 molar ratio in order to obtain ptsa-based eutectic mixtures.…”
Section: ■ Introductionmentioning
confidence: 99%
“…20 It is used in a very broad range of applications, e.g., as a catalyst, detergent solubilizer, resin hardener, in pharmaceuticals, or as an intermediate in the production of saccharine. 21,22 In the literature, different ptsa-based DESs have already been reported but barely characterized, e.g., ptsa:choline chloride at a molar ratio of 1:1, ptsa:benzyltrimethylammonium chloride at a molar ratio of 2.3:1, ptsa:allyltriphenylphosphonium bromide at a molar ratio 3:1, or ptsa:n,n-diethylenethanol ammonium chloride. 23−31 In this paper, combinations of ptsa with different HBAs were prepared in a 1:1 molar ratio in order to obtain ptsa-based eutectic mixtures.…”
Section: ■ Introductionmentioning
confidence: 99%
“…4 Conventional reactors, including tank reactors, thin-film reactors, falling film reactors, and jet loop reactors, have been employed in liquid−liquid heterogeneous reaction processes. 5,6 However, these reactors have some disadvantages especially when they are applied for highly exothermic and fast reaction systems. Insufficient heat-and mass transfer capabilities of these reactors may give rise to obvious gradients of concentration and temperature inside reactors, which may lead to low reaction rate, local overheating of reactors, formation of many impurities, or even runaway of the reaction.…”
Section: Introductionmentioning
confidence: 99%
“…In the first step, ethyl acetoacetate 2 and pyrazinamide 1 in presence 10 ml of glacial acetic acid reacted under neat conditions resulting in the formation of N -(3-oxobutanoyl)pyrazine-2-carboxamide 3 with the yield of 74%. The N -(3-oxobutanoyl)pyrazine-2-carboxamide was further taken for the Biginelli condensation reaction by reacting it with urea/thiourea and appropriate aldehyde in the presence of catalytic amount of laboratory made p -toluenesulphonic acid [30] . The advantages of the catalyst were better yields and do not require dry solvents.…”
Section: Resultsmentioning
confidence: 99%