dc.description.abstract | Phosphoric Acid Plant from Phosphoric Rock and Sulfuric Acid with a capacity of
60000 tons/year will be built in Gresik Industrial Estate, East Java with a land area of
26825 m2. The raw materials are Phosphate Rock obtained from Jordan Phosphate
Mines Ltd, Jordan and Sulfuric Acid from PT. Petrokimia Gresik, East Java. The
factory is designed to operate continuously for 328 days and requires 217 employees.
The reaction for making Phosphoric Acid begins with adding Phosphate Rock to the
Mixer (M-01) and mixing it with water. After that, feed the slurry of Phosphoric Rock
and Sulfuric Acid into the Stirred Tank Reactor (CSTR) which is arranged in series as
many as 2 pieces (R-01 and R-02) through the Heat Exchanger (HE-01) at a reactor
temperature of 80 oC and pressure 1 atm. This reaction takes place exothermic so it
requires water as a coolant to maintain the operating temperature. The product that
comes out of the reactor is a mixture of Phosphate Rock, Sulfuric Acid, Florida
Hydrogen, Gypsum, Phosphoric Acid and Water. The Florida hydrogen is routed to the
storage tank (T-02). While the mixture of liquid and solid phases then enters the Rotary
Drum Vacuum Filter (RDVF) to separate the Gypsum from the liquid phase. Then the
Gypsum is stored in the Warehouse (G-02) to be packed. While the liquid phase
mixture is flowed to the Evaporator (EV-01) to reduce the water content. After that, the
solution isflowed to the storage tank (T-03). The utility required by the Phosphoric Acid
factory is water taken from the Java Sea with a capacity of 192901.54 kg/hour.
Electrical power of 223556.39 kW is supplied from PLN. The need for fuel oil for
boilers is 1579845 kg/year, compressed air is 36.95 m3
/hour. The results of the
economic evaluation of this factory require that Fixed Capital Investment (FC) is IDR
5,139,570,041,066, Working Capital (WC) IDR 644,806,228,213, Manufacturing Cost
(MC) IDR 3,150,033,874,837, and General Expenses (GE) IDR 469,031,437,478. The
economic analysis shows the ROI before tax is 29.12% and the ROI after tax is 22%.
POT before tax is 3.43 years and POT after tax is 4.58 years. The BEP value is
30.022%, the SDP value is 19.18%, and the DCFR value is 25%. Thus, from a technical
and economic point of view, a Phosphoric Acid Plant from Phosphoric Rock and
Sulfuric Acid is worthy of consideration. | en_US |