Gas-Phase Preparation of Carbonic Acid and Its Monomethyl Ester

2014 ◽  
Vol 53 (44) ◽  
pp. 11766-11771 ◽  
Author(s):  
Hans Peter Reisenauer ◽  
J. Philipp Wagner ◽  
Peter R. Schreiner
2019 ◽  
Vol 26 (1) ◽  
pp. 285-305
Author(s):  
Eva‐Maria Köck ◽  
Jürgen Bernard ◽  
Maren Podewitz ◽  
Dennis F. Dinu ◽  
Roland G. Huber ◽  
...  

2014 ◽  
Vol 126 (44) ◽  
pp. 11960-11965 ◽  
Author(s):  
Hans Peter Reisenauer ◽  
J. Philipp Wagner ◽  
Peter R. Schreiner

2014 ◽  
Vol 126 (44) ◽  
pp. 11853-11853
Author(s):  
Hans Peter Reisenauer ◽  
J. Philipp Wagner ◽  
Peter R. Schreiner

2014 ◽  
Vol 53 (44) ◽  
pp. 11667-11667 ◽  
Author(s):  
Hans Peter Reisenauer ◽  
J. Philipp Wagner ◽  
Peter R. Schreiner

1991 ◽  
Vol 24 (7) ◽  
pp. 277-284 ◽  
Author(s):  
E. Gomólka ◽  
B. Gomólka

Whenever possible, neutralization of alkaline wastewater should involve low-cost acid. It is conventional to make use of carbonic acid produced via the reaction of carbon dioxide (contained in flue gases) with water according to the following equation: Carbon dioxide content in the flue gas stream varies from 10% to 15%. The flue gas stream may either be passed to the wastewater contained in the recarbonizers, or. enter the scrubbers (which are continually sprayed with wastewater) from the bottom in oountercurrent. The reactors, in which recarbonation occurs, have the ability to expand the contact surface between gaseous and liquid phase. This can be achieved by gas phase dispersion in the liquid phase (bubbling), by liquid phase dispersion in the gas phase (spraying), or by bubbling and spraying, and mixing. These concurrent operations are carried out during motion of the disk aerator (which is a patent claim). The authors describe the functioning of the disk aerator, the composition of the wastewater produced during wet gasification of carbide, the chemistry of recarbonation and decarbonation, and the concept of applying the disk aerator so as to make the wastewater fit for reuse (after suitable neutralization) as feeding water in acetylene generators.


2015 ◽  
Vol 12 (2) ◽  
pp. 236 ◽  
Author(s):  
Cristina Iuga ◽  
C. Ignacio Sainz-Díaz ◽  
Annik Vivier-Bunge

Environmental context The presence of air-borne mineral dust containing silicates in atmospheric aerosols should be considered in any exploration of volatile organic compound chemistry. This work reports the mechanisms, relative energies and kinetics of free-radical reactions with formic acid adsorbed on silicate surface models. We find that silicate surfaces are more likely to act as a trap for organic radicals than to have a catalytic effect on their reactions. Abstract Heterogeneous reactions of atmospheric volatile organic compounds on aerosol particles may play an important role in atmospheric chemistry. Silicate particles are present in air-borne mineral dust in atmospheric aerosols, and radical reactions can be different in the presence of these mineral particles. In this work, we use quantum-mechanical calculations and computational kinetics to explore the reaction of a hydroxyl free radical with a formic acid molecule previously adsorbed on several models of silicate surfaces. We find that the reaction is slower and takes place according to a mechanism that is different than the one in the gas phase. It is especially interesting to note that the reaction final products, which are the formyl radical attached to the cluster surface, and a water molecule, are much more stable than those formed in the gas phase, the overall reaction being highly exothermic in the presence of the surface model. This suggests that the silicate surface is a good trap for the formed formyl radical. In addition, we have noted that, if a second hydroxyl radical approaches the adsorbed formyl radical, the formation of carbonic acid on the silicate surface is a highly exothermic and exergonic process. The carbonic acid molecule remains strongly attached to the surface, thus blocking CO2 formation in the formic acid oxidation reaction. The spectroscopic properties of the systems involved in the reaction have been calculated, and interesting frequency shifts have been identified in the main vibration modes.


Author(s):  
A H J Maas ◽  
P Rispens ◽  
O Siggaard-Andersen ◽  
W G Zijlstra

This paper deals with the variability of the practical coefficient of the first ionisation equilibrium of carbonic acid as related to the CO2 in the liquid phase (Henderson-Hasselbalch equation) [Formula: see text] and that of the practical coefficient of the first ionisation equilibrium of carbonic acid as related to the CO2 in the gas phase (modified Henderson-Hasselbalch equation) [Formula: see text]


Science ◽  
1998 ◽  
Vol 279 (5355) ◽  
pp. 1332-1335 ◽  
Author(s):  
W. Hage
Keyword(s):  

2006 ◽  
Vol 2006 (5) ◽  
pp. 908-913 ◽  
Author(s):  
Angela Dibenedetto ◽  
Michele Aresta ◽  
Potenzo Giannoccaro ◽  
Carlo Pastore ◽  
Imre Pápai ◽  
...  

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