Phosphoric
Acid and the derived Phosphate fertilizers play an important role in any
economy which has substantial dependence on agriculture. India happens to be
one such country where agriculture contributes to approximately 17% of GDP and
employs somewhat more than 50% of India's employment.
Although I have never directly worked in the
fertilizer sector, I find this area of chemicals quite fascinating from a
chemical engineer's perspective. Lately I had been doing some studies on
production of wet phosphoric acid and the superphosphates. This led to my
developing a material balance spreadsheet for wet phosphoric acid production from
commercially mined phosphate rock which I am attaching with this blog entry
along with the reference of the literature I have used for developing this
spreadsheet. The spreadsheet also includes a process flow scheme for the
manufacture of wet phosphoric acid. But before I share the spreadsheet a brief
description of the process is essential. Here it goes:
Wet Process for Phosphoric Acid:
Phosphoric acid is produced from fluorapatite,
known as phosphate rock, 3Ca3(PO4)2.CaF2,
by the addition of concentrated (93%) sulfuric acid in a series of well-stirred
reactors. This results in phosphoric acid and calcium sulfate (gypsum) plus
other insoluble impurities. Water is added and the gypsum is removed by
filtration along with other insoluble materials (e.g. silica). Fluoride, as H2SiF6,
is removed at a further stage by evaporation. Although the reaction takes place
in stages involving calcium dihydrogenphosphate, the overall reaction can be
represented as:
However, there are side reactions; for example
with calcium fluoride and calcium carbonate present in the rock:
Fluorosilicilic acid is an important by-product
from this.
The crystal structure of the calcium sulfate
formed depends on the conditions of the reaction. At 340-350 K, the principal
product is dihydrate, CaSO4.2H2O. At 360-380 K, the
hemihydrate is produced, CaSO4.1/2H2O.
Calcium sulfate is filtered off and the acid is
then concentrated to 56% P2O5 using vacuum
distillation.
The product from the 'wet process' acid is
impure but can be used, without further purification, for phosphatic fertilizer
manufacture such as triple superphophate (TSP), Monoammonium
dihydrogenphosphate (MAP) and Diammonium hydrogenphosphate (DAP). Alternatively
it can be evaporated further to a concentration of 70% P2O5, a
solution called superphosphoric acid which is used directly as a liquid
fertilizer.