1000 k-g./ hour of ammonium bisulfate and 120 kg./hour of Water are fed to stirring vessel A via conduit 1, while a mixture of 2000 kg. of methanol
and 128 kg. of water is fed to the said vessel via conduit 3. 703 kg. of double salt,
consisting of 327 kg. of NH HSO 335 kg. of (NH SO 26 kg. of H 0 and 15 kg. of methanol, are separated off in filter device P. They are mixed with 415
kg. of water in stirring vessel B, and, after that, extracted with 2000 kg. of methanol and 128 kg. of water in stirring vessel C. 502 kg. of ammonium
sulfate, still containing 14 kg. of Water and 5 kg. of methanol, are separated off in filter device Q. This water and methyl alcohol are removed in
drying drum T, so that 483 kg. of ammonium sulfate are discharged via conduit 11.
Distillation of column X receives 2545 kg. of solution, consisting of 1985 kg. of methanol, 222 kg. of H 0 248 kg. of H 80 and 90 kg. of NH HSO via
conduit 13,
and, 2744 kg. of solution, consisting of I 2010 kg. of methanol 555 kg. of H 0,
110 kg. of H SO and 69 kg. of NH HSO via conduit 14.
The top product issuing from this column consists of 3995 kg. of methanol and 242 kg. of H 0. The bottom product, consisting of 1052 kg. of a solution
containing 40.5% by weight of H SO calculated to the sum of the free sulfuric acid and water presentand furthermore 15% by Weight of ammonium
bisulfate, is concentrated in distillation column Y.
540 kg. of sulfuric acid, contaminated with ammonium sulfate and being composed of 79.0% by weight of H 50 16.8% by Weight of (NH SO and 4.2% by
Weight of H 0 is discharged as bottom product. |