scholarly journals THE RATE OF CITRIC ACID FORMATION FOLLOWING THE INJECTION OF THE SODIUM SALTS OF CERTAIN DICARBOXYLIC ACIDS

1938 ◽  
Vol 124 (1) ◽  
pp. 43-48
Author(s):  
Arthur H. Smith ◽  
James M. Orten
1968 ◽  
Vol 46 (14) ◽  
pp. 2409-2413 ◽  
Author(s):  
Shmuel Migdal ◽  
David Gertner ◽  
Albert Zilkha

The controlled basic hydrolysis of tetrabutyl-1,3-dichlorodistannoxane under interfacial conditions was found to lead to α,ω-dichlorooligostannoxanes, Cl(SnBu2O)nSnBu2Cl, n being controlled by the molar ratio of base to distannoxane. These oligostannoxanes were identical with those prepared by other methods. They were used in the preparation of oligostannoxane dicarboxylates and organotin polyesters, having stannoxane recurring units in their backbone, by reaction with the sodium salts of mono- or dicarboxylic acids under interfacial conditions.


1966 ◽  
Vol 12 (5) ◽  
pp. 901-907 ◽  
Author(s):  
H. Horitsu ◽  
D. S. Clark

Ferrocyanide at concentrations of less than 30 p.p.m. (the amount tolerated in citric acid fermentation of beet molasses) had no measurable effect on citric acid production or on the oxidation of glucose or Krebs cycle compounds by resting cells of Aspergillus niger or on the growth rate of this organism during submerged fermentation of beet molasses. Concentrations above 30 p.p.m., however, stimulated citric acid formation in resting cells, but markedly inhibited cell development in growing cells. This inhibition of growth was the main cause of the detrimental effect of high concentrations of ferrocyanide on citric acid formation in molasses; good growth throughout the fermentation was essential to high acid yield, inhibition of growth could be released at any time during the fermentation by addition of sufficient ZnSO4 to reduce the ferrocyanide content to below 30 p.p.m. No evidence that ferrocyanide favors citric acid accumulation by blocking a reaction in the Krebs cycle was found.


1954 ◽  
Vol 32 (1) ◽  
pp. 68-80 ◽  
Author(s):  
Ping Shu ◽  
A. Funk ◽  
A. C. Neish

A medium containing glucose-1-C14 as the sole carbon source was fermented by Aspergillus niger under conditions giving a steady rate of oxygen consumption and a good yield of citric acid (63%). The citric acid was isolated and degraded by chemical methods to determine the carbon-14 concentration of the methylene carbons, the tertiary carbon, the tertiary carboxyl carbon, and the primary carboxyl carbons. These were found to contain, respectively, 35.6, 21.2, 7.25, and 5.99% of the C14 concentration of carbon-1 of the glucose. A mathematical analysis of these data in the light of current theories on citric acid formation suggested following conclusions: (a) 37–40% of the total citric acid was formed from recycled C4-dicarboxylic acid, (b) 40% of the dicarboxylic acid was formed through C2,C2 condensation and 60% through C1,C3 condensation, (c) 78% of the glucose was dissimilated through the Embden–Meyerhof scheme, the remainder being dissimilated through a mechanism involving carboxyl labeled pyruvic acid.


2019 ◽  
Vol 9 (1) ◽  
Author(s):  
Simon Carstens ◽  
Christian Splith ◽  
Dirk Enke

AbstractOne of the major routes to synthesize macroporous α-Al2O3 is the sol-gel process in presence of templates. Templates include polymers as well as carboxylic acids, such as citric acid. By careful choice of the template, pore diameters can be adjusted between 110 nm and several µm. We report the successful establishment of plain short-chain dicarboxylic acids (DCA) as porogenes in the sol-gel synthesis of macroporous α-Al2O3. By this extension of the recently developed synthesis route, a very precise control of pore diameters is achieved, in addition to enhanced macropore volumes in α-Al2O3. The formation mechanism thereof is closely related to the one postulated for citric acid, as thermal analyses show. However, since branching in the DCA-linked alumina nuclei is not possible, close monomodal pore width distributions are attained, which are accompanied by enhanced pore volumes. This is a significant improvement in terms of controlled enhanced porosity in the synthesis of macroporous α-Al2O3.


2019 ◽  
Author(s):  
Natalie R. Gervasi ◽  
David O. Topping ◽  
Andreas Zuend

Abstract. The viscosity of primary and secondary organic aerosol (SOA) has important implications for the processing of aqueous organic aerosol phases in the atmosphere, their involvement in climate forcing, and transboundary pollution. Here we introduce a new thermodynamics-based group-contribution model, which is capable of accurately predicting the dynamic viscosity of a mixture over several orders of magnitude (~ 10−3 to > 1012 Pa s) as a function of temperature and mixture composition, accounting for the effect of relative humidity on aerosol water content. The mixture viscosity modelling framework builds on the thermodynamic activity coefficient model AIOMFAC (Aerosol Inorganic–Organic Mixtures Functional groups Activity Coefficients) for predictions of liquid mixture non-ideality, including liquid–liquid phase separation, and the calorimetric glass transition temperature model by DeRieux et al. (2018) for pure-component viscosity values of organic components. Comparing this new model with simplified modelling approaches reveals that the group-contribution method is the most accurate in predicting mixture viscosity, although accurate pure-component viscosity predictions (and associated experimental data) are key and one of the main sources of uncertainties in current models, including the model presented here. Nonetheless, we find excellent agreement between the viscosity predictions and measurements for systems in which mixture constituents have a molar mass below 350 g mol−1. As such, we demonstrate the validity of the model in quantifying mixture viscosity for aqueous binary mixtures (glycerol, citric acid, sucrose, and trehalose), aqueous multicomponent mixtures (citric acid + sucrose and a mixture of nine dicarboxylic acids), and aqueous SOA surrogate mixtures derived from the oxidation of α-pinene, toluene, or isoprene. We also use the model to assess the expected change in SOA particle viscosity during idealized adiabatic air parcel transport from the surface to higher altitudes within the troposphere. This work demonstrates the capability and flexibility of our model in predicting the viscosity for organic mixtures of varying degrees of complexity and its applicability for modelling SOA viscosity over a wide range of temperatures and relative humidities.


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