SULPHUR
HANDLING TERMINAL IN RUWAIS
Brief
Process Description
Sulphur Handling Facility consists of
following four functional units
Liquid sulphur storage and offsites
Liquid sulphur delivered by road tankers of 30 tons is unloaded to sulphur
unloading pit which is transported to liquid sulphur storage tank by the pit
pump. All liquid sulphur unloading or transfer line is steam jacketed to
maintain the liquid sulphur temperature of 135 C with low pressure steam to
prevent liquid sulphur from freezing.
Liquid sulphur in liquid sulphur storage tank is pumped to sulphur day pit
through sulphur filters by sulphur transfer pump, from where the sulphur is
pumped to granulation units.
Granulation
A total of nine granulation units have been installed with a capacity of
approx 1000 Tons/day. Each granulator is provided with its own dedicated wet
scrubber.
Exhaust vapours form the new granulators is burnt at the incinerator.
Marine terminal
Marine terminal is used to unload liquid sulphur coming from Janana shipment
form ADGAS. Approx. 8000 Tons is unloaded and transferred to storage tanks.
Hydraulic control system is used to operate to unloading arm.
Solid sulphur storage, handling and utilities.
Sulphur product from granulators is collected at collecting conveyors
equipped with dust collection system and transferred to a bulk storage building.
There are two bulk storage buildings circular type of 40,000 Tons of capacity
and linear type of 110,000Tons of capacity. There is also a facility to load
sulphur granules onto a truck. Granulated sulphur is exported to ships through
the shiploader system on a conveyor at the rate of 1000 Tons/hr.
Wet Scrubbers :
Granulators
The Sulphur granulation units rely on a stream of cool, humid air to cool and
solidify the solid sulphur. Since the air stream leaving the granulators is
vented to atmosphere, the potential exists for discharge of particular sulphur.
To reduce the level of particular sulphur emitted, the granulaotrs are
equipped with a wet scrubbing system on the effluent air system.
Conveying system dust collectors
During the normal course of handling solid sulphur, some sulphur dust will be
generated. To keep this dust from accumulating within the conveyors and causing
mechanical problems, the conveyor enclosures are swept with air. The dust is
entrained into thte air stream. This dust laden air system, if vented directly,
would be a major source of particulate emissions.
Therefore all conveyors are equipped with dust collection systems.
Liquid Sulphur Feed Characteristics as per the
Engineering data
Purity |
dry wt. Basis |
99.8 % |
H2S |
ppm wt. Less than |
10 |
Arsenic |
|
nil |
Selenium |
|
nil |
Tellurium |
|
nil |
Ash ppm wt. Less than |
|
500 |
Carbon ppm wt. Less than |
|
500 |
Molecular weight (S-32) |
|
256 |
Boiling point, C (atmos. Pr.) |
|
444 |
Freezing point c |
|
115 |
Explosive limits of dust in air, clouds C |
|
190 |
Corrosiveness |
|
Dry sulphur is non-corrosive, but attacks steel readily in the presence of moisture. |
Solubility |
|
Soluble in carbon disulfide, carbon tetrachloride, benzene slightly soluble in alcohol and ether, insoluble in water. |
Reactivity |
|
Moderately reactive burns to form sulphur dioxide. Mixtures with chlorates, nitrates or other oxidizing agents may be explosive. Reacts with alkalizes and earth’s. |
Solid Sulphur Product specification
Characteristics as per the Engineering data
Color |
Bright yellow |
Bulk density |
1040 to 1200 kg/m3 |
Surface Moisture ppm(Wt) |
5000 |
Angle of repose |
25 |
Friability test |
Fines generated 70% of time max 3% wt. |
|
Fines generated 90% of time max 3.5% wt. |
Size Distribution |
|
Max % of granules retained on 4.7mm screen |
5.0 Wt % |
Fines – 300 u |
0.5 Wt % |
Compaction Fines |
0.2 Wt % |
SULPHUR
PRODUCTION
Principle of Operation
Sulphur granulation is a size enlargement process by which liquid sulphur is
sprayed onto a "core" or "seed" materisl and cooled to
solidification before the next coat of liquid is added. Through repeated
application of liquid sulphur, the seed increases in volume and weight. Each
granule is formed through step-enlargment and, therefore, the granules grow in
size to reach optimum dimensions for handling, transportation and friability. As
the granule enlarges, the liquid sulphur sprayed onto the smaller seed granule
is bonded before the next coating is applied. This elimates the inherent
shrinkage effect of sulphur during the solidification stage and ensures that the
process provided a granule that is spherical, dry and completely free of voids.
The size-enlargement process occurs in a rotating drum. This drum serves as a
tumbling bed, a liquid sulphur spray booth and controlled heat removal area.
Seed cores, consisting of fines and undersized, recycled granules, are fed to
the sulphur-granulating drum at a predetermined rate. Travelling down the length
of the drum due to positive displacement, the seed is lifted by flights on the
inside of the periphery of the drum. As the drum rotates, the seed particles are
lifted vertically and dropped from approximately the twelve o’clock position,
which results in the formation of a thick, falling curtain. Liquid sulphur is
sprayed onto the falling curtain by a series of spray nozzles which are located
along the length of the drum and which operate at pre-set pressures. An air
blower pulls air through the drum to provide a cooling medium for the
granulating drum as seed material.
The GX systems uses ambient air as the cooling medium and the volume of air
pulled through the drum can varied depending on ambient temperatures. In
addition, the utilization of air inside the drum is enhanced through the use of
cross-fans which serve several functions. Firstly each fan agitates the air
which is travelling down the length of the drum, creating a spiral effect. The
air comes into contact with the granulating product and the humidification
system several times throughout its journey. Secondly the GX process contains an
arrangement to humidify the cooling air and this humidified air is drawn by the
fans and blown onto the falling curtain, which creates and evaporative cooling
effect on the granules. The method of heat extraction is very efficient and the
level of humidification can be adjusted to reflect local ambient conditions.
Enlarged granules emerging from the granulating drum are deposited onto a
vibratory screen separator where the granules are segregated into product and
undersize granules. The product size granules are taken out of the processing
area to storage. The undersize particles are directed to the granulating rum for
further size enlargement. The screening procedure will control the finished
product size and this aspect of the GX process can be adjusted to provide the
customer and end user with the size distribution required.
GRANULATION DRUM
SHIPLOADER