ELECTROLYTIC IRON POWDER FROM SPONGE IRON FINES

PLANT PARAMETERS

Capacity

2000 kg/per day

No.of Shifts  per day

2

Working days per Year.

300

Land Area, m2

3000

Covered Area, m2

2500

MANPOWER

Technicall

15

Skilled

20

Unskilled

20

RAW MATERIAL/DAY

Sponge iron fines,             2500 kg

Hydrochloric acid             25000 ltrs

Ammonium Chloride (commercial)

Nylon/Polypropylene cloth

Chemicals required for washing

Ammonia or NaOh to control pH

Chemicals for analysis

UTILITIES/DAY

Power

4400 KWH

Water, Steam etc.

80 m3

PLANT & MACHINERY

Rectifier 5000 A-60 with substation        

Centrifuge, Furnace                                               

Concrete tanks with FRP lining               

FRP support for anodic  bag                

Electrolyte filtration unit, Scrappers                        

Overhead crane to handle electrodes    

Weighing machine              

Ameter 0-5000A                                     

INTRODUCTION

Iron powder is mainly produced by the reduction of its oxide using Hoganas and Pyron process, water atomization of low-carbon iron, QMP process, Domfer process, carbonyl vapor metallurgy process, by electrolysis process, fluidised-bed reduction process and by H-iron ONIA process. The iron powder applications comprise for cutting and scarfing, making welding electrodes, the manufacture of powder metallurgy and for food enrichment.

USES   The Product is used for automotive and other industries, welding electrode, flame cutting and scarfing, in chemical industries, frictional materials, abrasive wheel and cutting tubes etc.

PROCESS

The production of Electrolytic Iron powder from sponge iron fines involves using sponge iron fines – 3 mm size typically comprising Fe:88-91%; Fe0:5.0-6.0%; C:0.20-0.25%; S:0.02-0.03%; P:0.05-0.07%; Mn:Trace;SiO2 + Al2 O3 :5.0 -6.0% as soluble anode placed inside a porous diaphragm made of nylon or poly-propylene. The electrolyte of the cell consists of a novel composition of ferrous chloride and ammonium chloride (commercial grade). The proposed combination of the chemicals helps attain higher electrical conductivity of the electrolyte. The current drawn from a DC source is passed through the specially designed anode. The cell electrodes comprise an anode of sponge iron fines placed inside a porous diaphragm nylon or polypropylene mentioned as above and fastened with an insoluble multiple titanium strips (CP grade) for contact and cathode of stainless steel onto which the EIP gets deposited during the electrolysis process.

SPECIFICATIONS

Carbon : 0.005%; Silica:0.020%; Manganese: Trace; Sulphur:0.003%; Phosphorus:0.003%; Acid Insolubles:0.02-0.08%; Hydrogen Loss:0.08 – 0.15%. The physical properties of the powder exhibits Apparent density as 2.2 – 3.1g/cm3 ; flow rate as 25/30; Compressibility (4.2t/cm2) as 6.8 – 7.0; Green Strength as 24-25 (2.45 cm OD x 1.8cm ID Bush).

The sieve analysis of the powder conforming to BS is as given below:

BS SieveNo.

+100

+150

+240

+300

+350

20

Percentage

Nil

20

25

20

-350

15

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(A Government of India Enterprise)
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