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Simplot Phosphoric Acid Purification Process
The Research and Development Department of the J. R.
Simplot Company has successfully developed a membrane based system for the
purification of wet process phosphoric acid after four years of intensive
research. A first-of-a-kind, 30,000 t/y solution purification plant using this
technology successfully started up in 1996 to produce high quality, fertigation
(drip) grade phosphoric acid.
Process Advantages
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A high
value added product is manufactured from wet process phosphoric
acid.
-
No
solvents are used in the process.
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Commercially proven.
-
Only
by-product is a raffinate acid stream.
-
Low
capital and operating costs.
-
Produces
a technical grade acid.
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Available
through a licensing agreement with KEMWorks Technology.
-
Process
is flexible - high levels of product quality can be met through multiple stages
of membrane filtration.
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Simple,
easy to operate process.
Process Description.jpg)
In the
Simplot phosphoric acid purification process, a high quality purified phosphoric
acid is produced from wet process phosphoric acid using a proprietary membrane
based process. This process is novel and unique, and unlike other purification
processes is not based on solvent extraction.
The phosphoric acid feed
stock to this process is either 30%, 42% P2O5 or higher strengths wet process
phosphoric acid. This feed acid is cooled and, if necessary, reacted with a
suitable calcium source such as finely ground phosphate rock or lime to reduce
sulfate levels to less than 0.25%. The acid is then filtered to remove gypsum
and other suspended solids.
The clean phosphoric acid filtrate is
pressurized and fed to an ultrafiltration system to remove the suspended solids
by cross-flow membrane filtration. Approximately 95% of the feed acid is
recovered as an ultrafiltration permeate. This ultraclean, solids free permeate
is pressurized using centrifugal or positive displacement pumps and filtered
using proprietary membranes that remove 99+% of all metallic
constituents.
Following the phosphoric acid purification step, the
purified produce acid is concentrated in a forced circulation evaporator to 50
to 54% P2O5. The raffinate acid, that contains all the removed impurities, may
be concentrated by evaporation. The raffinate, containing all the rejected
impurities, is utilized in the production of single or triple superphosphate,
16-20-0, or mono-ammonium phosphate (MAP).
|
Constituent |
Feed Acid
(%) |
Product Acid (%)
** |
|
P2O5 |
43.5* |
54.5 |
|
F |
1.5 |
<150ppm |
|
Al |
0.44 |
<30ppm |
|
Fe |
0.33 |
<20ppm |
|
Mg |
0.57 |
<50ppm |
|
Cr |
450ppm |
<3ppm |
|
Ca |
250ppm |
<10ppm |
|
V2O5 |
1500ppm |
<25ppm |
|
Cd |
125ppm |
<5ppm |
* 42% or,
alternatively, 30% P2O5 feed acid may be used as feed stock to
process. ** Product quality
produced with a two-stage membrane purification process using phosphoric acid
produced from Idaho uncalcined
rock.
Raw Materials, Utilities, etc.
|
Typical Raw Material
Consumption |
Per ton
purified P2O5 |
|
Feed acid (as 42% P2O5
or 50% P2O5) Phosphate rock (or other calcium source) Process
water |
1.43 tons
P2O5 <0.08 tons CaO 2.0 tons water |
|
Products and
by-Products |
Per ton
purified P2O5 |
|
Product acid (as
54%P2O5) Raffinate acid (as 30% P2O5) Waste water (with 1%
P2O5) |
1.0 tons P2O5 0.4
tons P2O5 0.1 tons |
|
Utilities |
Per ton
purified P2O5 |
|
Low pressure
steam Electricity Cooling water |
3.9 tons 270
KWh 200 tons |
|
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