The
ash slurry pumps for combined B.A. and F.A. disposal, B.A. Cooling
water over flow pumps, BAHP pumps, BALP pumps, flushing water pumps
seal water pumps, for ash slurry pumps, dust suppression, ash
conditioning and seal water pumps in main storage silo area and
cooling water pumps for cooling various equipments of ash handling
plant shall essentially be horizontal and centrifugal type. The
equipment shall be capable of developing the required head at rated
capacity for continuous operation.
All
Centrifugal
Pumps shall have a drooping characteristics
curve, with the head continuously increasing with decreasing flow to
maximum head at zero flow and the pumps shall preferably be
non-overloading type beyond rated duty point. The characteristics
curves of each set of pumps shall match each other for equal load
sharing in case of parallel operation and such pumps shall be
identical and all parts shall be fully interchangeable.
The
ash slurry sump geometry and configuration shall be such as to
minimise ash settlement, formation of vortices and air entrainment in
the slurry as this may affect the operation of the slurry disposal
pumps. To minimise the ash settlement adequate number of high
velocity water jetting nozzles shall be provided in the slurry sumps.
The
fly ash slurry concentrations under this mode of operation shall be
decided, considering the rated capacity of the extraction system. To
maintain the concentration limit and to run the ash slurry disposal
pumps efficiently a provision shall be made for make-up water pipe
connections complete with motor operated gate valves and manual gate
valves.
Minimum
10% margin shall be considered for ash slurry pump sizing over and
above the total slurry disposal head requirement comprising the
straight pipe line frictional loss and bends loss. The value of the
constant ‘C’ in William-Hazen equation shall be considered as 140
for calculating the system head.
An
additional flow of 100 m³/hr (continuous) shall be considered on ash
slurry pump capacity to take into account sludge disposal from
clarifier units to be pumped by ash slurry disposal pumps to the
disposal area. Bidder may take advantage of this additional quantity
of sludge (the density of solids in sludge may be taken as 1.1 and
the concentration as 5%) while arriving at ash slurry concentration
for the combined ash disposal pumps. Apart from the working streams
one standby and one maintenance standby shall be provided for the ash
slurry disposal system.
The
slurry pumps shall essentially be slow rpm pumps. The rotational
speed of the impeller at design point shall not exceed 1000 rpm. The
first stage of slurry disposal and transportation pumps shall be
provided with variable speed hydraulic coupling of robust design for
setting the optimum operating speed of the pumps based on actual site
requirements after the system is installed. Minimum (+) 10% and (-)
45% speed variation with respect to speed at rated design point
shall be provided in the first stage of combined ash slurry disposal
pumps and ± 20% for bottom ash transportation and BA overflow water
pumps. The slurry pump motor speed shall not exceed 1500 rpm.
To
minimise the drive losses in the first stage of slurry disposal and
transportation pumps, a constant speed reduction gear box shall be
provided. The gear boxes to be employed shall be suitable for heavy
duty application and of such reputed make which have proven
established record of trouble free service under heavy load
transmission duties.
For
the subsequent slurry disposal and transportation pump stages, the
drive shall be transmitted through belt drive arrangement. If in
future, the operating speed of these pumps is also required to be
changed, the Owner intends to carry out this change by replacing the
existing belt-pulley with a pulley of different diameter to allow a
future variation of ± 10%. Pump and motor layouts in the pump house
shall be accordingly decided to take care of this requirement.
Continuous
motor rating (name plate rating) at 50°C for ash slurry pumps shall
have at least 20% margin above the maximum load demand of the driven
equipment at the rated duty point. The maximum load demand shall be
calculated considering slurry density, efficiency of pump when
handling slurry and the complete drive losses in the transmission
(fluid coupling, gear box, etc.). For selecting the motor, the
maximum pump efficiency to be considered shall be 70%. To ensure
interchange ability, all the pumps & motors of the pumping
streams shall be of similar rating and the pumps shall be designed
for + 10% and – 45% speed variation.
Pumps
shall be single stage, end suction design provided with heavy duty
impellers suitable for highly abrasive duty application. All the wear
parts of pumps, impellers and liners etc. shall have a minimum
guaranteed life of 8000 hrs. of operation. Provision shall be made
for adjustment to take up wear by axial movement of the shaft. The
seals shall be water flushed packed glands, fed from an external
clean water supply source. The impeller tip speed at the rated
parameters shall not be more than 1676 metres/min. Bidders shall
make selection of the pump size such as to limit the tip speeds to
above specified limits. The passages and clearances in pump
components shall be properly designed, considering the size of ash
and clinker to be handled.
The
pumps shall have flooded suction inlet and shall be located indoors.
However, pumps shall be suitable for operating with up to 2 metres
suction lift. The glands of the pumps should be suitably designed to
prevent clogging of ash particles.
About
Us :
Everest
Industries is a leading Centrifugal
Pump and Plate Lifting Clamp supplier
and manufacturer
in Ahmedabad, Gujarat, India. Centrifugal pumps are a sub-class of
dynamic axisymmetric work-absorbing turbomachinery.
Contact
Detail :
Telephone:
+9179-22902552
E-mail:
everestind2552@yahoo.co.in
FAX:
+91-9427710684
For
more information, please visit Everest Industries Website
everestindustries.co.in
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