Chemicals Based
Technologies - Bromine from Sea Water
Introduction
Bromine is widely distributed in nature,
but in relatively small proportions. Bromine and bromo-compounds
have wide range of uses in chemical and other uses.
It is used for the manufacture of dye intermediate &
dye stuffs, drugs & pharmaceutical products, photography
chemicals, insecticides, fuming agents, antiknock gasoline,
fire retardants, in textile industry and in oil exploration.
It is also used in controlling microbes and algae in
swimming pools.
The bromine available for extraction occurs as bromide
in the ocean, in salt lakes and in brine or saline deposits
left by evaporation of such waters by solar heat. Sea
bitterns, the left over concentrated solution after
the crystallizing out of salt from the sea water, are
very reach in bromine and offers a good raw material
for the manufacture of bromine. Sea bittern having at
least 2.2 gm/lit bromine , is most suitable for the
manufacture of bromine. The technology for manufacture
of bromine has been developed at Central Salt and Marine
Chemical Research Institute, Bhavnagar, India and the
technology has been licensed to 9 salt manufacturers
and five of them are in production. The capacity utilization
of these plants during the last ten years was noticed
to be varying between 30 % to 70 % and their total production
always remained far below the demand of bromine in the
country. The total demand of bromine for the year 2000
AD has been projected to be 700- 800 tonnes and to meet
the requirement of bromine in the country ,the production
capacity of the country has to be increased by at least
60 %. Therefore the production of bromine offers a good
prospects to those entrepreneurs who has access to sea
bittern.
Process
The 30o Be' bittern from the reservoirs
is taken in sump tank and then fed to the chlorinating
tower. After perchlorination, the cold bitterns is preheated
by hot recycle brine and the fed at the top of a stripping
tower wherein steam is introduced at the bottom to further
heat the bittern to boiling point and strip the bromine
liberated by chlorine. Sulfuric acid is also added to
the tower to facilitate stripping of bromine. The liberated
bromine with excess steam is passed through the two
stage condenser to separate steam and uncondensed bromine
and chlorine gas mixture is scrubbed in the chlorinating
tower. The crude bromine is separated from water in
gravity separator and further purified by fractional
distillation and passing through sulfuric acid column.
The water condensed overhead of stripping tower and
the impure gas emerging from the distillation column
are recycled. The debrominated effluent brine is treated
with caustic soda and is used for pre-heating chlorinated
bittern.
Plant Parameters
Capacity, TPA
150
No.of Shifts / day
3
Working days / Yr.
300
Land Area, m2
4000
Covered Area, m2
600
Manpower
Managerial
9
Skilled
15
Unskilled
26
Raw Material
(Tonne per Tonne
of Product)
Sea bitterns
4.33
Sulphuric acid
0.002
Chlorine
0.004
Caustic soda
0.002
Utilities (Per Tonne of Product)
Power, KwH
10
Water, KL
1
Steam, Tonnes
0.27
Coal , Tonnes
0.05
Plant & Machinery
Bittern preheater
Separator
Stripping tower
Level gauges
Steam condenser
Boiler
Bromine condenser
Flow meters
Distillation column
Br. cooler
For further information please
contact :
National Research Development Corporation
( A Government of India Enterprise )
20-22, Zamroodhpur Community Center
Kailash Colony Extension
New Delhi 110 048. India
Tel: 91-11-26419904, 26417821, 26480767, 26432627
Fax: 011-26231877, 26460506, 26478010
Website: www.nrdcindia.com