| 摘要 |
1,037,526. Drying chlorine. KONINKLIJKE NEDERLANDSCHE ZOUTINDUSTRIE N.V. May 1; 1964 [June 14, 1963], No. 18217/64. Heading B1L. Gaseous chlorine is dried by a process wherein the gas is subjected to one or more cooling steps and to two or more drying steps using sulphuric acid as the drying agent but withdrawing the acid and the gas separately from each step. The last or only cooling step is combined with the first drying step and the gas is cooled in the presence of the acid by heat exchange with an evaporating liquid. In a specific embodiment, Fig. 2, gaseous C12 which may be preliminarily cooled to not lower than 10‹C. and freed from condensed water, is supplied to Venturi tube 8. Sulphuric acid enters tube 8 by conduit 9 and the gas/acid mixture passes to heat exchanger 11. Conduit 12 introduces the gas mixture into vessel 13 below the level of the diluted H2SO4 which is cooled by coil 14 and overflows at 15. Chlorine is discharged from 13 into conduit 16 and heat exchanger 11 and passes on to vessel 18 which is fed with cone. H2SO4, oleum or liquid SO3 by conduit 20. Dry chlorine leaves at 19 while discharged acid passes along conduit 9 to tube 8. In an alternative embodiment, Fig. 3, gaseous chlorine enters at 2 while conc. H2SO4 enters at 4. Dried chlorine leaves at 3 and spent sulphuric acid leaves at 5. Acid from the lowest tray may be withdrawn and cooled to -30‹C. by cooler 22 whilst in the tray above, the acid is heated at 24 to prevent formation of a solid sulphuric acid hydrate. In another embodiment (Fig. 1, not shown) liquid C12 is fed to the tower just above the point of entry of the gaseous chlorine, thus effecting cooling of the gaseous Cl2 in the presence of the acid. An advantageous condition is that the temperature of the gaseous chlorine in the first drying step be lower than that at which chlorine hydrate will be formed but prior to or during a subsequent drying step the gas is heated to a temperature higher than that at which solid sulphuric acid hydrate will be formed. |
