ChemInform Abstract: MECHANISM OF CARBON DIOXIDE ELIMINATION FROM IONIZED METHYL HALOACETATES IN THE GAS PHASE. FORMATION OF CH3XCH2+.CNTDOT. AND CH3XCHX+.CNTDOT. (X = CL, BR) HALONIUM RADICAL IONS

1983 ◽  
Vol 14 (31) ◽  
Author(s):  
Y. APELOIG ◽  
B. CIOMMER ◽  
G. FRENKING ◽  
M. KARNI ◽  
A. MANDELBAUM ◽  
...  
1983 ◽  
Vol 105 (8) ◽  
pp. 2186-2193 ◽  
Author(s):  
Yitzhak Apeloig ◽  
Bernhard Ciommer ◽  
Gernot Frenking ◽  
Miriam Karni ◽  
Asher Mandelbaum ◽  
...  

2017 ◽  
Author(s):  
Robson de Farias

<p>In the present work, are calculated the gas formation enthalpies (SE; PM3 and PM6) for tin borates: SnB<sub>2</sub>O<sub>4</sub><sup> </sup>and Sn<sub>2</sub>B<sub>2</sub>O<sub>5</sub>. The calculated values are compared with experimental ones, obtained by Knudsen effusion mass spectrometry [3]. It is shown that SE methods, besides their lower computational time consuming can, indeed, provide reliable gas phase formation enthalpy values for inorganic compounds containing heavy metals.</p>


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.


Studies of the catalytic oxidation of benzene to maleic anhydride and carbon dioxide over vanadia/molybdena catalysts show that the major part of the reaction involves interacting gas and gas-solid processes. The results are consistent with a mechanism in which a benzeneoxygen adduct is formed catalytically, desorbs and then reacts to give maleic anhydride entirely in the gas phase. On the basis of this proposed mechanism, the kinetics of individual reactions have been investigated in some depth. The over-oxidation of maleic anhydride has been found to be not significant under the conditions of reaction. The kinetic relationships governing the homogeneous decomposition of the adduct and the oxidation of the adduct to maleic anhydride and to carbon dioxide have been established. The results show that essentially all of the anhydride originates from mixed gas-solid/gas reaction while substantial amounts of carbon dioxide are produced entirely catalytically.


2008 ◽  
Vol 47 (47) ◽  
pp. 9118-9121 ◽  
Author(s):  
Charlene C. L. Thum ◽  
George N. Khairallah ◽  
Richard A. J. O'Hair
Keyword(s):  

1987 ◽  
Vol 15 (10) ◽  
pp. 944-946 ◽  
Author(s):  
SHUJI DOHI ◽  
REIKO TAKESHIMA ◽  
NAOKI MATSUMIYA

1999 ◽  
Vol 185-187 ◽  
pp. 25-35 ◽  
Author(s):  
Detlef Schröder ◽  
Christoph A Schalley ◽  
Jeremy N Harvey ◽  
Helmut Schwarz

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