Lanthanum nitrate → Ammonia

FIGURE shows an embodiment of the process according to the invention. The sodium zeolite is treated in an ion exchanger stage first with an aqueous ammonium carbonate solution, then with an aqueous lanthanum nitrate solution. Thereafter, treated zeolite and mother liquor are separated by a suitable process, for example filtration, and optionally dried. The zeolite thus pretreated is calcined in a furnace, releasing ammonia. These stages can be conducted twice or more in succession. The mother liquor from the removal stage is supplied to a column which comprises a stripping section and is heated at the bottom with an evaporator or by direct addition of steam. The temperature increase drives out ammonia and carbon dioxide, entraining water in the form of steam. The vaporous mixture is condensed in a direct or indirect condenser, and ammonia and carbon dioxide recombine with water to give aqueous ammonium carbonate. The ammonium carbonate solution thus obtained is recycled into the ion exchange stage. Via the bottom of the column, an aqueous sodium carbonate solution is discharged. The ammonia from the calcining furnace is optionally conducted with supplementary ammonia and carbon dioxide into the column upstream of the condenser.

1. customoptionally dried
2. customThe mother liquor from the removal stage
3. temperatureis heated at the
4. custombottom with an evaporator
5. additionby direct addition of steam
6. temperatureThe temperature increase
7. customcondensed in a direct or indirect condenser

ORD-Eintrag

ord-019694a9d217468fae709a643eeba0a8

Quelldatensatz

uspto-grants-2016_09

DOI

10.6084/m9.figshare.5104873.v1

Patentnummer

US09446960B2