METHODS FOR PRODUCING UREA CALCIUM SULFATE FROM MOIST PHOSPHOGYPSUM
Method for producing a urea calcium sulfate (UCS) adduct is disclosed. The method for producing the UCS adduct, includes contacting urea with a moist phosphogypsum containing 10 wt. % to 30 wt. % of moisture, under conditions sufficient to form a slurry comprising formed UCS adduct.
1 . A method for producing a urea calcium sulfate (UCS) adduct, the method comprising:
(a) contacting urea with a moist phosphogypsum comprising 10 wt. % to 30 wt. % of moisture, under conditions sufficient to form a slurry comprising formed UCS adduct.
2 . The method of claim 1 , wherein an aqueous urea solution is contacted with the moist phosphogypsum to form the slurry.
3 . The method of claim 2 , wherein the formed slurry comprising formed UCS adduct comprises 10 wt. % to 30 wt. % of water.
4 . The method of claim 1 , wherein urea particles having a size of 0.1 mm to 1 mm are contacted with the moist phosphogypsum to form the slurry.
5 . The method of claim 1 , wherein urea granules and/or prills having a size of 1 mm to 4 mm are contacted with the moist phosphogypsum to form the slurry.
6 . The method of claim 1 , wherein the contacting conditions in step (a) include a temperature of 40° C. to 80° C.
7 . The method of claim 1 , wherein the moist phosphogypsum contacting the urea has a temperature of 30° C. to 60° C.
8 . The method of claim 1 , further comprising obtaining the moist phosphogypsum from a phosphoric acid manufacturing plant prior to step (a).
9 . The method of claim 8 , wherein:
i) the moist phosphogypsum produced from the phosphoric acid manufacturing plant is not dried and/or pretreated to reduce moisture content of moist phosphogypsum below 10 wt. % prior to contacting the urea in step (a) and/or
ii) wherein no water is added to the moist phosphogypsum produced from the phosphoric acid manufacturing plant after production of the phosphogypsum or in the contacting step (a) other than the water contained in the moist phosphogypsum from the phosphoric acid manufacturing plant.
10 . The method of claim 8 , wherein the moist phosphogypsum produced from the phosphoric acid manufacturing plant is not cooled to a temperature below 30° C. prior to contacting the urea in step (a).
11 . The method of claim 1 , wherein a molar ratio of urea contacting the moist phosphogypsum to calcium sulfate contained in the moist phosphogypsum contacted in step (a) is 1:0.25 to 1.2:0.16.
12 . The method of claim 1 , further comprising:
(b) drying the slurry to form a dried fertilizer composition comprising the formed UCS adduct.
13 . The method of claim 12 , wherein the dried fertilizer composition comprises 0 wt. % to 10 wt. % of moisture.
14 . The method of claim 12 , wherein the drying in step (b) comprises contacting the slurry or a dryer used for drying the slurry with steam.
15 . The method of claim 12 , wherein 40 wt. % to 95 wt. % of the dried fertilizer composition is comprised of the formed UCS adduct.
16 . The method of claim 1 , further comprising granulating the formed UCS adduct before, during, and/or after drying the slurry.
17 . The method of claim 16 , wherein the granulating is performed in a granulator and step (a) is performed in a vessel different from the granulator.
18 . The method of claim 17 , wherein the granulating comprises contacting the formed UCS with steam or the granulator used for granulating the formed UCS with steam.
19 . The method of claim 1 , wherein the slurry of step (a) further comprises a base and/or a urease inhibitor.
20 . The method of claim 1 , wherein the method further comprises combining the formed UCS adduct with at least one additional fertilizer to form a fertilizer blend and/or compounded fertilizer.