Mostrando 1 - 4 Resultados de 4 Para Buscar 'Gómez R., Héctor', tiempo de consulta: 0.01s Limitar resultados
1
artículo
By using the criterions of sensibility of IUPAC, we had determinad the sensibility far chromic (III) and (VI) from solution of its differents salts. We found that ion chromic (VI) in the form ion chromate is much sensible than chromic (III).
2
artículo
By using the criterions of sensibility of IUPAC, we had determinad the sensibility far chromic (III) and (VI) from solution of its differents salts. We found that ion chromic (VI) in the form ion chromate is much sensible than chromic (III).
3
artículo
Applying the method of pressure swing distillation (PSD) we obtained (97 % v/v) ethanol starting from 95 % v/v ethanol, which shows that the ethanol-water azeotrope has been broken in this study. Experimental work to achieve the final product was carried out operating !he column in two stages or modes, these being: (1) Low pressure distillation (LPD), and (2) High pressure distillation (HPO). In the first operating mode, a low degree industrial alcohol (80 % v/v ethanol) is fed to a bench scale distillation column packed with Mellapack structure, where (95 % v/v) ethanol is obtained, working at atmospheric pressure. Then product collected in !he first stage is fed to the reboiler, and !he HPD process takes place to get 97 % (v/v) ethanol. Here we have shown that it is possible to perform the pressure swing using an auxiliary engineered device, instead of using a second distillation colum...
4
artículo
Applying the method of pressure swing distillation (PSD) we obtained (97 % v/v) ethanol starting from 95 % v/v ethanol, which shows that the ethanol-water azeotrope has been broken in this study. Experimental work to achieve the final product was carried out operating !he column in two stages or modes, these being: (1) Low pressure distillation (LPD), and (2) High pressure distillation (HPO). In the first operating mode, a low degree industrial alcohol (80 % v/v ethanol) is fed to a bench scale distillation column packed with Mellapack structure, where (95 % v/v) ethanol is obtained, working at atmospheric pressure. Then product collected in !he first stage is fed to the reboiler, and !he HPD process takes place to get 97 % (v/v) ethanol. Here we have shown that it is possible to perform the pressure swing using an auxiliary engineered device, instead of using a second distillation colum...