Continuous phosphate crystallization system and phosphate manufacturing method
By integrating a monoammonium phosphate (MAP) production system and an integrated continuous crystallizer, the entire process of phosphate production is automated, solving the problems of high equipment investment, large footprint, and unstable products in existing technologies, and achieving efficient and low-cost phosphate production.
WO2026144388A1PCT designated stage Publication Date: 2026-07-09WUHUAN ENG
Patent Information
- Authority / Receiving Office
- WO · WO
- Patent Type
- Applications
- Current Assignee / Owner
- WUHUAN ENG
- Filing Date
- 2025-10-14
- Publication Date
- 2026-07-09
Smart Images

Figure CN2025127496_09072026_PF_FP_ABST
Abstract
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.
Need to check novelty before this filing date? Find Prior Art