A continuous
phosphate crystallization system and a
phosphate manufacturing method. The continuous
phosphate crystallization system comprises a monoammonium phosphate production
system (100), an integrated continuous crystallizer (7), a
crystallization circulation pump (9), a crystallization heater (10), a crystallization vacuum condensation system (11), a crystallization material pump (12), a thickener (13), and a
centrifuge (15), wherein a
raw material input end of the integrated continuous crystallizer (7) is configured to be connected to a
raw material phosphoric acid of a second concentration and an
ammonia gas, or to be connected to a monoammonium phosphate
slurry output end of the monoammonium phosphate production system (100), a circulating material output end of the integrated continuous crystallizer (7) is connected to a circulating material input end by means of the crystallization circulation pump (9) and the crystallization heater (10) in sequence, a crystallized material output end is connected to an input end of the
centrifuge (15) by means of the crystallization material pump (12) and the thickener (13) in sequence, and the
centrifuge (15) outputs a phosphate to be dried. The method comprises: delivering a
raw material phosphoric acid of a first concentration in the range of 40-58% to the monoammonium phosphate production system (100) to obtain flash steam and a monoammonium phosphate
slurry, and delivering the monoammonium phosphate
slurry into the integrated continuous crystallizer (7) to obtain a crystallized material; or, delivering a raw material
phosphoric acid of a second concentration in the range of 75-85% and an
ammonia gas into the integrated continuous crystallizer (7) to obtain a crystallized material; and sequentially performing thickening,
centrifugation and
drying on the crystallized material to obtain a phosphate.