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Oxidation of methyl mercaptan

Manufacture. Methanesulfonic acid is made commercially by oxidation of methyl mercaptan by chlorine in aqueous hydrochloric acid to give methanesulfonyl chloride which is then hydrolyzed to MSA. [Pg.154]

Oxidation of Mercaptans by O Oxidation of methyl mercaptan in aqueous solution by 03 produces methane sulfonic acid as the major product. The reaction mechanisms are complex with the formation of dimethyl disulfide (CH3SSCH3), methyl methane thiolsulfonate (CH3S02SCH3), and methyl methanethiolsulfinate (CH3SOSCH3) as minor products. Continued ozonation could result in slow formation of sulfuric acid ... [Pg.545]

All the results described above led to the conclusion about the importance of surface chemistry for adsorption/oxidation of methyl mercaptan. The dependence of the amount of methyl... [Pg.277]

Chemical/Physical. In the presence of nitric oxide, gaseous methyl mercaptan reacted with OH radicals forming methyl sulfenic acid and methyl thionitrite. The rate constant for this reaction is 2.1 X 10 cmVmolecule-sec at 20 °C (MacLeod et al., 1984). [Pg.776]

Further routes of cyclizations have been studied in parallel in the case of cis- and rra/J5-2-hydroxymethyl-l-cyclohexylamine (106) (880PP73). The preparation of thiourea or urea adducts 107 and 108 with phenyl isothiocyanate or phenyl isocyanate proceeds smoothly. The reaction of 107 with methyl iodide and subsequent alkali treatment, by elimination of methyl mercaptan, resulted in the iminooxazine 109 in high yields. The ring closures of both cis and trans thiourea adducts to 1,3-oxazines proceed with retention. Cyclodesulfuration of the adduct 107 by mercury(II) oxide or N,N -dicyclohexylcarbodiimide resulted in the iminooxazine 109, but the yield was low and the purification of the product was cumbersome. The ring closure of 108 with thionyl chloride led to the iminooxazine 109 in only moderate yield. [Pg.366]

The impact of MOX upon reductive odors was included in the study of McCord (2003) for MOX at 5-10 mL/L/month over 5 months on a Cabernet Sauvignon wine in commercial scale tanks. Lower concentrations of methyl mercaptan and ethyl mercaptan were observed in the oxygenated wines, but no impact was seen upon disulfides, in spite of the suggestion that concentrations of the disulfides could increase due to direct oxidation of sulfides. Dimethyl sulfide concentrations were not affected, except that lower concentrations were seen in wines with added toasted oak staves or segments, with or without MOX. The concentrations of various oak extracted compounds were also measured in this study, with similar levels seen with and without MOX alongside appreciable increases due to the presence of the oak staves or segments in some cases (e.g., lactones and vanillin), oxygenation appeared to enhance aroma extraction. [Pg.172]

Adsorption of methyl mercaptan in moist conditions was performed on numerous samples of activated cartons of various origins. Methyl mercaptan adsorption was tested by a dynamic method. The amount of products of surface reaction was evaluated using thermal analysis. The results revealed that the main product of oxidation, dimethyl disulfide, is adsorbed in pores smaller than SO A. There is apparent competition for adsorption sites between water (moist conditions) and dimethyl disulfi. The comp ition is won by the latter molecule due to its strong adsorption in the carbon pore system. Althou dimethyl disulfide has to compete with water for the adsorption sites it can not be formed in a significant quantity without water. Water facilitates dissociation of methyl mercaptan and thus ensures the efficient removal process. [Pg.141]

The amount of methyl mercaptan (MM) adsorbed (and converted to dimethyl disulfides (DMDS) depends on the sur e pH [ 1, 2], and the presence of various impregnants, such as potassium iodide, potassium iodite, potassium carbonate or ammonia [3,4], It has also been pointed out in the literature that different functional groups on the carbon sur ce or/and metal ions such as iron can catalyze oxidation of mercaptans to disulfides [3-6]. As we have found recently, there is an indication of a competition for high-energy adsorption sites between dimethyl disulfide and water molecules when adsorption occurs in the presence of moisture [1,2]. This happens as a result of big differences between water and DMDS in the strength of adsorption forces and their incompatibility (DMDS has very low solubility in water) [7]. [Pg.141]

An objective of this paper it to describe the results of our further investigation of the competition for adsorption sites between water and dimethyl disulfide molecules during methyl mercaptan adsorption on activated carbons. Moreover, we attempt to indicate the apparent borderlines between the conditions of adsorption processes leading to different adsorption/oxidation paths. Those working conditions have a significant effect on the feasibility of methyl mercaptan removal. [Pg.141]

The aromas associated widi very fi esh fish are usually mild, delicate and fi esh (53,54), and generally described as green (hexanal), melon-like ((E,Z)-3,6-nonadienal), iodine-like (bromophenols). Fresh fish and seafood aromas are due to volatile carbonyls and derive fi om lipoxygenase catalyzed oxidation of polyunsaturated fatty acids. The oxidation of Eicosapentaenoic acid (C20 5) leads to C5 to C9 alcohols, aldehydes, ketones and hydrocarbons. The formation of methyl mercaptan, dimethyl sulfide and dimethyl disulfide in fi esh fish at the time of harvest has been reported by Shiomi et al. (55). Although these compounds are usually associated with fish deterioration, they contribute to the fi esh aroma ch cter at low concentrations. For instance, dimethyl sulfide is... [Pg.15]

A well-known example of a complex catalytic reaction that takes place on the surface of carbon is the oxidation of hydrogen sulfide [329,330], When water is present on the carbon surface and the surface has the basic pH required for dissociation of H2S, oxidation of the HS ions by active oxygen occurs either to elemental sulfur or sulfuric acid. The latter is formed when the reaction takes place in very small pores, where only sulfur radicals very susceptible for further oxidation to SO3 are formed. Catalytic oxidation also occurs in the case of methyl mercaptan adsorption [331], where on basic carbon, thiolate ions formed as a result of dissociation are further oxidized to dimethyldisulfide strongly adsorbed in the pore system. In the case of desulfurization, inorganic constituents of carbon such as iron and calcium also play a crucial role. Those elements, present even in small amounts, contribute significantly to the oxidation reactions as catalysts [332,333],... [Pg.81]

A thiourea such as (311) was oxidized with sodium molybdate and hydrogen peroxide to an amidine sulphonic acid (312). The sulphonic acid group was replaced by an amine to give the guanidine Scheme 5.70.) [374]. The avoidance of methyl mercaptan as a by-product was a considerable advantage. [Pg.262]

Moroxydine (512) was first synthesized by introducing morpholine to dicyanodiamidine [667], but an improved method is the oxidation of amidinothiourea (510) with hydrogen peroxide and sodium molybdate dihydrate to give (511) followed by reaction with morpholine [374] Scheme 5.120.). This avoids the evolution of methyl mercaptan. The drug has antibiotic properties and some action as an influenza suppressant [668]. [Pg.300]

The significance of industrial acrolein production may be clearer if one considers the two major uses of acrolein—direct oxidation to acryUc acid and reaction to produce methionine via 3-methyhnercaptopropionaldehyde. In acryUc acid production, acrolein is not isolated from the intermediate production stream. The 1990 acryUc acid production demand in the United States alone accounted for more than 450,000 t/yr (28), with worldwide capacity approaching 1,470,000 t/yr (29). Approximately 0.75 kg of acrolein is required to produce one kilogram of acryUc acid. The methionine production process involves the reaction of acrolein with methyl mercaptan. Worldwide methionine production was estimated at about 170,000 t/yr in 1990 (30). (See Acrylic ACID AND DERIVATIVES AmINO ACIDS, SURVEY.)... [Pg.124]

Through reaction with sulfide or elemental sulfur at 215°C, lignosulfonates can also be used in the commercial production of dimethyl sulfide and methyl mercaptan (77). Dimethyl sulfide produced in the reaction is further oxidized to dimethyl sulfoxide (DMSO), a useful industrial solvent (see Sulfoxides). [Pg.144]


See other pages where Oxidation of methyl mercaptan is mentioned: [Pg.145]    [Pg.272]    [Pg.145]    [Pg.1029]    [Pg.145]    [Pg.272]    [Pg.145]    [Pg.1029]    [Pg.1580]    [Pg.141]    [Pg.145]    [Pg.374]    [Pg.319]    [Pg.276]    [Pg.277]    [Pg.181]    [Pg.198]    [Pg.198]    [Pg.141]    [Pg.145]    [Pg.462]    [Pg.190]    [Pg.130]    [Pg.200]    [Pg.396]    [Pg.268]    [Pg.269]    [Pg.74]    [Pg.347]    [Pg.874]    [Pg.52]    [Pg.57]    [Pg.98]    [Pg.100]    [Pg.103]    [Pg.105]   
See also in sourсe #XX -- [ Pg.248 ]




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Mercaptan

Mercaptane

Mercaptanes

Mercaptanes oxidation

Mercaptans

Mercaptans methyl

Mercaptans, oxidation

Methyl 3-oxid

Methyl oxide

Methyl, oxidation

Oxidation of mercaptans

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