Sulphuric acid, theoretical studies

The photochemistry of ethyl esters of 2-oxo-carboxylic acids has the participation of both singlet and triplet excited states o. Triplet state lifetimes have been measured and the occurrence of Norrish type II splits in these molecules established. Other flash photolysis studies reported deal with the photoinduced tautomerism of 2-hydroxyphenazine °, 3-methylisoxazolo[5,4-b]pyridine °, and the photolysis of 4,4 -biphenylbiazide °. The tautomerism and phototautomerization of 4(3H)-pyridinethione has been examined theoretically by the infra red isolation technique . The effect of pressure on the photoinduced abstraction reaction of azanaphthalenes in mixed crystals of durene has also been studied. Photosolvolysis of arylmethanols also occurs in aqueous solutions of sulphuric acid . 

Accurate knowledge of solution density is important in calculating theoretical energy density values of flow battery electrolytes and for pump selection during battery system design. The results obtained in this study showed that the viscosity and conductivity of vanadium (IB) sulphate solutions are more sensitive to changes in the solution s chemical composition compared to the density of the solution. The present studies showed that the density of vanadium (III) sulphate solutions is directly proportional to the concentration of vanadium (III) sulphate and to a lesser extent to the concentration of sulphuric acid. The density of the solution decreased slightly with the increase in the solution s temperature. 

PETP flakes produced from used soft drinks bottles were subjected to alkaline hydrolysis in aqueous sodium hydroxide. A phase transfer catalyst (trioctylmethylammonium bromide) was used to enable the depolymerisation reaction to take place at room temperature and under mild conditions. The effects of temperature, alkali concentration, PETP particle size, PETP concentration and catalyst to PETP ratio on the reaction kinetics were studied. The disodium terephthalate produced was treated with sulphuric to give terephthalic acid of high purity. A simple theoretical model was developed to describe the hydrolysis rate. 17 refs. 

The alkylation, with the more reactive of alkyl halides, of the sodium salts of monoes-terified phosphonothioic acids (equation 22) (see also Scheme 11) or of the disodium salts 107 results in preferential S-alkylation, and the same situation obtains for the salts of phosphinothioic acid " methylation can also be carried out with dimethyl sulphate. Alkylations may also be performed under phase-transfer conditions. From both practical and theoretical perspectives, the subject is more complex, since the course of alkylation reactions depends on the nature of the alkylating agent, on the polarity of solvent and whether this is protic or non-protic and on the concentrations of reactants a study of these features has been the subject of two reports In non-polar or weakly polar aprotic media, or in EtOH, alkylation occurs almost exclusively on sulphur, but in dipolar aprotic solvents, O-alkylation also takes place. The relative yields of sulphur- and oxygen-substituted derivatives, [Qs/Qol depends, for a given solvent, on the nature of substituents on phosphorus, i.e. essentially, whether the substrate is a thiophosphoric, thiophosphonic or thiophosphinic acid. With alkyl tosylates as alkylating agents at 0.02 m in hmpt, the alkylation of sodium 0,0-dialkyl or diphenyl phosphorothioates results in 100% overall conversions with [Qs/Qo] 5 the overall yields for sodium diphenyl- or diisopropyl-phosphinothioates are lower (50-100%) with [Qs/Qo] 1 ... 

The major limitation in sulphur recovery was due to the fact that the recovered stream consisted of 65% of CO2, and 35% of H2S. If richer with H2S, then recovery should theoretically increase. The specific recommendation made for this issue were as follows (i) to inject the acid gas after liquefaction in deep geological formation into natural gas reservoir, (ii) to separate the CO2 from the feed so that it is rich in H2S while CO2 is being injected to the gas reservoir, (hi) to separate the CO2 from the feed before entering the recovery imit in order to enhance the recovery. A viable solution to the C02 issue in the case study would be to utihze it as a feed stock for methanol production in another facility. 

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