ELECTROLYTIC CHROMIUM METAL

PLANT PARAMETERS
Capacity, TPA 100 200
No.of Shifts / day 3 3
Working days / Yr. 300 300
Land Area, m 2 2500 10000
Covered Area, m2 1100 3800
MANPOWER
Managerial 2 3
Skilled 10 12
Unskilled 12 16
RAW MATERIAL
(Tonne per tonne of Product)
Chromic acid 2.1
Sulphuric acid 0.008
Copper sheet 0.4
Nitric acid 2.5
UTILITIES(Per Tonne of Product)
Power, KwH 120,000
Process Water, KL 110
Raw Water, KL 150
PLANT & MACHINERY
Rectifier Transformer
FRP lined PVC cells Blowers
Titanium heat exchanger Busbar & connectors
Mixing tanks Effluent treatment tank
S.S. Ball mill Cooling tower
Chromium is the 21st element in the earth's crust in relative abundance. Although it was first isolated and indentified as a metal as early as in 1798, its early application was in the form of chromium compounds in pigments and tanning of leather, but its use as an alloying element, was gradually developed during the 19th century.The metal exhibits excellant properties of oxidation resistance, hardenability and corrosion resistance. While the major applications of chromium metal flkes are in production of high alloy steels, super alloys for high temperatures and heating elements, fluxes, coins; the use of chromium metal powder, at present, is largely confined to the manufacture of welding electrode manufacturing industries.where it is used for production of certain types of stainless steel electrodes to compensate for welding losses.

The chromium metal can be manufacture either by alumino thermic process or by electrochemical process . The metal produced by the former process are less pure and has limited application than that produced by the electrchemical. route .However, the electrochemical process is power intensive and therefore proper consideration should be given in selecting the location of the plant for adequte supply of power at less price.

PROCESS

Chromium metal is produced by the electrolysis of commercial grade chromic acid. The steps involved in the process are :

a)Preparation of the electrolytic bath solution -The chromic acid is mixed thoroughly with demineralised water in the mixing tank to form a uniform solution having concentration of 250 gm/litre. Proper protection should be taken since chromic acid is very much corrosive. Required amount of sulphuric acid is added to the solution so keep the sulphate ion concentration level at 2.5 gm/litre.

b)Electrolysis of Chromic acid Solution - The solution thus prepared is fed to the electrolytic cell. The cells are made of PVCwith FRP lining having Pb-Ag (99:1) alloy anodes and stainless steel cathode. The cathodes are treated separately before putting inside the cell for chromic acid electrolysis. The cell liquid temperature is maintained at around 39oC by circulating cell liquid through titanium heat exchanger. The cell voltage. cathode current density are maintained at the appropriated value.

After 24 hrs. of cell operation the cathodes are taken out of the cell, washed with the demineralised water. The deposits of chromium from the cathode are peeled off followed by treating with nitric acid to remove the adherent impurities, washing with water and finally drying. The dried chromium flakes are sold if required or it is ground in a stainless steel ball mill to desired particle size.

Specification of Chromium metal powder

Chemical Analysis Sieve Analysis
Element % Mesh (ASTM) %
Cr, Min 98.0 + 60 Nil
Fe, Max 1.0 - 60 + 100 0.50
Al, Max 0.10 - 100 + 200 70.0
Si, Max 0.20 - 200 + 325 20.0
C, Max 0.10 - 325 10.0
P, Max 0.05    
S, Max 0.04    

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