AMMONIA HEATING GROUP FOR MELAMINE PRODUCTION PLANTS AND MELAMINE PRODUCTION PLANT USING THE SAME
A heating group for melamine production plants and a melamine production plant using the heating group. The heating group for melamine plants comprises a molten salt circuit for supplying the reaction heat to the plant and a superheated ammonia supply unit comprising at least an evaporation exchanger and a superheating exchanger, the superheating exchanger comprising at least one separate heat source with respect to the molten salt circuit, the separate heat source being superheated steam. The superheating exchanger is a jacketed tube of two concentric tubes wherein the inner tube is suitable for a flow of ammonia to be superheated and the sealed outer tube or jacket is suitable for a flow of superheated steam, the inner tube having an internal diameter which ranges from 20 mm to 85 mm, corresponding to a length of the jacketed tube ranging from 30 to 20 m.
1 . A heating group for melamine production plants comprising a circuit of molten salts for supplying the reaction heat to a melamine production plant and a superheated ammonia supply unit to said plant, said unit comprising at least one evaporation exchanger and a superheating exchanger, wherein:
the superheating exchanger comprises at least one separate heat source with respect to the molten salt circuit, said separate heat source being superheated steam;
said superheating exchanger comprises a jacketed tube comprised of two concentric tubes wherein an inner tube is configured for a flow of ammonia to be overheated and a sealed outer tube or jacket is configured for a flow of superheated steam; and
said internal pipe has an internal diameter which ranges from 20 mm to 85 mm, corresponding to length of the jacketed tube ranging from 30 m to 20 m respectively.
2 . The heating group for melamine production plants according to claim 1 , wherein the inner tube has an internal diameter ranging from 21.6 mm to 55 mm, corresponding to a length of the jacketed tube ranging from 27 m to 23 m.
3 . The heating group for melamine production plants according to claim 1 , wherein the exchanger is thermally coupled with a heat source independent of the molten salt circuit.
4 . The heating group for melamine production plants according to claim 1 , wherein said heat source of the superheating exchanger is superheated steam flowing in the outer tube constituting the jacket about the inner tube in which ammonia flows.
5 . The heating group for melamine production plants according to claim 1 , wherein the inner tube in which ammonia flows is made of an ammonia-resistant material.
6 . The heating group for melamine production plants according to claim 1 , wherein the evaporation exchanger uses steam available in the melamine production plant as heating fluid.
7 . The heating group for melamine production plants according to claim 1 , wherein said molten salt circuit comprises a circulation pump, a molten salt tank and a heating furnace, the circulation pump creating at least a flow of molten salts from the tank to the heating furnace, from the heating furnace to the reactor and from the reactor to the tank without passing through said superheating exchanger.
8 . A plant for the production of melamine comprising at least one reactor for the production of melamine from urea and a heating group for supplying, at least to said reactor, the reaction heat and superheated ammonia according to claim 1 .
9 . The heating group for melamine production plants according to claim 1 , wherein the inner tube has an internal diameter ranging from 24.6 to 50.8 mm, corresponding to a length of the jacketed tube ranging from 25 m to 22 m.
10 . The heating group for melamine production plants according to claim 5 , wherein the inner tube in which ammonia flows is made of an alloy with a high nickel content.