 |
Expansion of the 1 million tpy
Jaypee Rewa
Cement Plant, India
| P. G. Sogani
General manager: Engineering
Holtec Engineers Private
Ltd.
New Delhi, India |
S. K. Gupta
Senior manager: Engineering
Holtec Engineers Private
Ltd.
New Delhi, India |
| 1.) Introduction
Jaypee Rewa Cement (JRC),
a division of Jaiprakash Industries Limited (JIL), commissioned their first
1 million tpy cement plant at the end of 1986. This was carried out less
than 30 months from the date of placement of the order for the main plant
and machinery. An article by the author on this plant, was published in
World Cement's January/February 1987 issue, entitled 'India adds yet another
one million tpy cement plant'.
Having successfully commissioned
the first unit (Unit 1), JIL contemplated the expansion in less than a
year. At that point of time the cement industry was at a relatively low
ebb and talk of expansion was considered daring. However, the management
was confident of the cement industry's future in the growing Indian economy
and decided to proceed. The expansion was planned for the same premises,
with provision for this expansion being available in the original plant
layout.
The company placed orders
for supply of main plant and machinery in April/May, 1989. The clinkerisation
unit of the new plant (Unit 2) designated at 1.2 million tpy capacity was
commissioned in April 1991 (less than 24 months from the date of order
placement). The new cement grinding and packaging facilities are currently
being commissioned (completion expected before March 1992).
The engineering and consulting
services for this Rs. 1740 million expansion project were provided jointly
by Holtec Engineers Private Ltd., New Delhi, and their associates Holderbank
Management & Consulting Limited (HMC), Switzerland. By present day
standards this would be one of the most economical and quickly installed
projects of such a large capacity in India.
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2.) Infrastructure
Most of the infrastructure
has remained unchanged from that built for Unit 1. However, suitable additions
have been provided for the increased requirements in respect of roads,
power supply and water. Even today, the plant does not have a railway siding
on site. Its own small railway siding is at Satna, about 50 km away. The
rail link to the plant is presently under construction and is expected
to be commissioned in 1992. The nearest airports are at Khajuraho and Allahabad,
about 175 and 135 km from the plant respectively. |
| 3.)
Raw materials
JIL possess two limestone
deposits at Naubasta which is adjacent to the plant and Bela which is at
a distance of 4 km from the plant.
Holtec carried out a detailed
geological investigation of both these limestone deposits utilizing the
latest state-of-the-art computer based techniques, i.e. CADE (Computer
Aided Deposit Evaluation) in collaboration with HMC. The application of
CADE established:
-
the existence of sufficient
quantity of the required quality limestone in the two deposits, based on
analysis of deposit block models constructed through application of geostatics.
-
optimized quarry schedules,
based on the required raw mix parameters of the cement plant, for ease
of mining operation.
-
substantial increase in limestone
reserve estimates due to optimized exploitation envisioned through CADE.
-
the relatively economical cost
of homogenized run-of-mine production.
The geological setting, though
rather complex, permits fully mechanized open cast mining at both the blocks.
At Naubasta, the blasted
limestone is transported by 3.2 m³ hydraulic excavators and 35 t dumpers,
to a stationary crusher situated within the plant.
At Bela, the blasted limestone
is fed to the mobile crusher by a similar 3.2 m³ hydraulic excavators
and 35 t dumper combination. The crushed limestone is transported to the
plant by a bi-cable aerial ropeway.
The envisaged raw mix consists
of 98% run-of-mine limestone and 2% laterite/iron ore.
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4.) Plant design
The entire plant design and
engineering was carried out with the objective of ensuring trouble free,
smooth operation and adequate inter changeability between Units 1 and 2
to achieve sustained high levels of production. Some of the unique methodology
and technological aspects adopted are outlined below:
Methodology:
-
The main machinery suppliers
were invited by the company to visit their operating plant and assess the
various strengths and weaknesses of the existing facilities/systems for
themselves. During their visits, the suppliers received operational feedback
from plant personnel and management.
-
The consultants' specialist
team carried out a plant audit of Unit 1 with a view to obtaining first-hand
feedback on plant operation and constraints so that this information could
be utilized in improving Unit 1 as well as designing Unit 2.
-
Basic engineering viz. main
machinery tender specifications, plant layout and GA drawings were jointly
conceived at HMC headquarters in Switzerland by HMC, Holtec and JRC.
-
Main machinery and auxiliary
equipment package selection resulted from a series of discussions between
the purchaser, the consultants and the suppliers. The selection package
devised was such that it enabled the company to purchase equipment best
suited to its technical and economic requirements.
Technological Aspects:
-
Ease of operation and maintenance.
-
Optimizing conveying distances
and manpower requirements.
-
To keep the investment low,
wherever possible, existing systems were upgraded to make them suitable
for both Units 1 and 2 requirements e.g.
-
Naubasta limestone crusher capacity
planned for upgradation.- The capacity of the limestone preblending stockpile
stacker unit, upgraded from 700 tph to 1400 tph.
-
Stockpile storage capacity was
also increased from 2 x 30 000 t to 4 x 35 000 t by adding a new reclaimer
and associated belt conveyors.
-
The existing 2 x 100 tph capacity
open circuit cement mills were made closed circuit by incorporating High
Efficiency Separators (HES), thereby increasing the system capacity to
2 x 155 tph.
-
The existing mechanical rotary
packers replaced by more modern electronic versions.
-
Inter changeability between
Units 1 and 2 has been ensured at all process sections so that the effect
of down- time of critical equipment in both the units is minimal for sustained
plant output.
-
Raw material hoppers of short
duration storage capacity coupled with the mass flow design of hoppers
and their extraction systems have been installed to ensure trouble- free
operation.
-
The latest state-of-the-art,
on-line bulk analyser and sampler system is being installed between the
limestone crusher and the preblending stockpile to facilitate the optimizing
of mining operations and minimize quality variations for the kiln.
-
Extensive use of the most efficient
pollution control equipment in the plant both for production units as well
as material handling transfer
points, to meet forthcoming stringent pollution control regulations.
-
To overcome the feeding problems
of pozzolana in case of grinding of Portland Puzzolana Cement (PPC) with
trunnion bearing mills, a slide shoe bearing cement mill has been selected.
Central drive in place of conventional twin drive has been selected for
energy saving.
-
The use of a fully mechanized
bridge type bucket chain stacker reclaimer system using a pit for storage
of pozzolana and gypsum.
-
The installation of new additional
electronic rotary packers in conjunction with curved belt conveyors and
fast loading machines, thereby avoiding any fall of cement
bags during transfer from packers to trucks.
-
QA centralized yet distributed,
closed loop, computerized process control system.
-
Captive diesel generating sets
(3 x 5.8 MW) to be provided to ensure uninterrupted operation of critical
equipment in case of power shortages/cuts from the state grid; bringing
the total captive power generation capacity for both Units 1 and 2 to over
29 MW. In view of the current deterioration in grid power availability,
this was a very prudent managerial decision.
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General arrangement
drawing
Process
flow diagram
| 5.) Plant equipment
The broad specifications
of major equipment and its respective supplier(s) are tabulated in Table
1 below:
| Department |
Equipment specification |
Supplier |
| Limestone
crusher |
Naubasta Crusher: (existing)
APPM 1822 Single Rotor Impactor for Unit 1, planned for upgradation from
650 t/h to 900 t/h |
Larsen&Toubro,
India |
| |
Bela Crusher: (existing-no
modification) Single Rotor Impactor, APPM 1822, 650 t/h, 780 kW on a tyre
mounted chassis |
Crusher:
Larsen&Toubro, India
Chassis: Krupp, Germany |
| Limestone
preblending |
Existing inline rectangular
stockpile from 2 x 30.000t to 4 x 35.000 t by adding reclaimer and upgrading
stacker capacity from 700 t/h to 1.400 t/h |
Modifications/new
reclaimer from CIMMCO, India |
| Raw
material grinding |
Vertical Roller Mill, LM
50.4, 5.000 kW drive (max. cap. 400 t/h) |
LOESCHE,
Germany
CIMMCO, India |
| Raw
meal homogenizing & kiln feed |
Continous flow silo, 23.500
t x 1 RCC Silo, 22,4 m dia, Gravimetric kiln feed through Airlift pumps |
F.L.
Smith, Denmark
Larsen&Toubro, India |
| Clinker
burning |
5-stage preheater with separate
line precalciner 4,75 m dia x 75 m long rotary kiln, 750 kW drive, reciprocating
grate cooler, 130 m² grate area (max. cap. 4.500 t/day. |
-
do - |
| Clinker
transport and storage |
1 No. deep Drawn pan conveyor,
375 t/h, conical covered stockpile of 16.000 t capacity. Provision for
Clinker silo in near future |
Aumund,
Germany
(through FLS) |
| Coal
grinding |
Vertical Roller Mill, LM
26.3D,
780 kW drive (max. cap.
55 t/h) |
LOESCHE,
Germany
CIMMCO, India |
| Cement
grinding |
Existing modified:
2 x 100 t/h existing open
circuit mills modified to close circuit with HES to 2 x 155 t/h capacity,
2 x 2.400 kW drive |
Modifications
by Fuller KCP India
|
| |
New mill:
1 x 185 t/h close circuit
mill with HES, 4,8 m dia. x 15,75 long, slide shoes bearings, Central drive,
5.000 kW drive |
Mill
by Fuller KCP, India
Central drive by Maag Switzerland |
| Cement
storage |
4 x 5.000 t RCC silos (modifications
for interchangeability)
New: 2 x 5.000 t RCC Silos |
F.L.
Smith Denmrk Larsen&Toubro India |
| Cement
packing |
Existing: (modified)
4 x 60 t/h, 14 spout mechanical
rotary packers, with curved belt conveyors and fast loading machines for
trucks |
Haver
Boecker make, supplied by Enexco, India |
| |
New: 3 x 120 t/h, 8 spout,
twin outlet, electronic rotatry packers with curved belt conveyors and
fast loading machines for trucks. |
-
Do - |
| Coal
crusher |
Roll crusher, 250 t/h,
110 kW drive |
Larsen&Toubro, India |
| Coal
stockpile |
Existing: (no modification)
27.000t rectangular stockpile, slewing type stacker 250 t/h, portable side
chain scraper type reclaimer 200 t/h |
-- |
| Gypsum/puzzolana
storage |
16.000 t Gypsum, 4.000 t
Puzzolana pit storage, bridge type, stacker with bridge type chain bucket
reclaimer, stacker 350 t/h, reclaimer 150 t/h |
MVT,
Germany
CIMMCO, India |
| On-Line
bulk material analyser |
PNAA type 200 t/h with automatic
sampler (split type from 1.400 t/h to 200 t/h) |
Sampler
MVT, Germany
Analyser: Gamma (PNAA) Metrics,
USA |
| Pollution
control equipment |
ESP´s:
(outlet emission 150 mg/Nm³)
One each for:
-
kiln, raw mill
-
coal mill
-
coller
-
cement mill-3
|
F.L.
Smith Denmrk Larsen&Toubro India
Cement mill-3: Fläkt,
India |
| |
Bag Filters:
(outlet emissions 50 mg/Nm³)
45 nos. at various locations |
GEC-India |
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6.)
Electrical, power, control and instrumentation
The total connected load
of Unit 2 is around 30 MVA and the estimated power demand is 26 MVA. This
demand is the same as that for Unit 1, despite the higher plant capacity
because many of the existing facilities are common and some are upgraded
to meet the expanded requirements.
The existing 132 kV switchyard
has been upgraded to take care of the additional loads of Unit 2.
Power is distributed within
the plant through the following 5 load centres at either 6.6 kV for HT
motors or 415 V for LT motors.
-
Load Centre 1: At crusher section
(existing)
-
Load Centre 2: At raw mill and
kiln section
-
Load Centre 3: At cooler and
coal mill sections
-
Load Centre 4: At cement mill
and packing sections
-
Load Centre 5: At quarry (existing)
Here are about 700 motors in
the plant. The major electrical equipment has been procured from the following
Indian suppliers:
132 kV switchyard expansion,
Bharat Bijlee
6.6 kV motors, BHEL
6.6 kV switchboards, Asea
Brown Boveri
Distribution transformers,
415 V LT switchboards, Motors control centres, Crompton Greaves
LT motors, SPRS transformers,DC
motors, Kirloskar Electric
Thyristor converter panels,
Larsen & Toubro
Slip power recovery system,
Asea Brown Boveri
3 x 5.8 MW diesel generating
sets Wartsila, Finland
The complete control and
instrumentation packages have been procured from Asea Brown Boveri Ltd.,
India (a subsidiary of ABB-Sweden) who had supplied a similar package for
Unit 1. For efficient operation, the entire plant has been provided with
integrated and distributed digital controls for centralised automatic operation
from the following four control centres:
-
Limestone crushing
-
Clinkerisation from central
control room-2 (CCR-2)
-
Cement grinding from central
control room-1 (existing CR-1)
-
Packing and despatch
CCR-2 is located in the existing
CCR building on the same floor as that of CCR-1. The cement mill of Unit
2 has been connected to CCR-1 for better coordination of the entire cement
grinding operation.
The entire plant operation
for clinkerisation has been divided between two supervisory processors
in CCR-2. However, in the event of failure of one processor, plant operation
can be carried out from the other without interruption.
For raw mix control, the
existing on-line X-ray spectrometer system along with microprocessor based
computer PDP-11123 installed in the main CCR building, will be used for
manual correction of the set points of the raw mill weighfeeders.
The total length of power,
control and instrumentation cables is about 400 km.
Preheater tower
(Unit 2) and blending silos (Units 1 and 2)
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| 7.) Civil works
Most of the civil works were
carried out by one of the group companies of JIL except for certain slipform
works for the blending silo, cement silos and ESP columns for which M/s
Bygging India were engaged. The quantities of the civil work involved in
the execution of the Unit 2 is outlined below (excluding the housing colony
and other amenities where only marginal additions have been done):
-
Excavation: 95.000 m³
-
Plain concrete: 12.000 m³
-
Reinforced concrete: 50.000
m³
-
Formwork: 130.000 m²
-
Reinforcement steel: 7.500 t
-
Structural steel: 6.000 t
-
Cement: 22.000 t
Some of the special conditions
and features from the view point of civil engineering design and construction
during the execution are highlighted below. These are unique in nature
and also helped expedite construction:
-
Due to the rocky sub-soil strata,
special techniques and efforts were deployed for blasting (muffled blasting)
so that the adjoining existing plant structure foundations (of Unit 1)
were not affected.
-
Highly mechanised civil construction
was adopted involving use of earth moving machinery for excavation, batching
plant for concrete making, transit mixers, concrete pumps, tower crane
(700 m height) etc. Extensive use was made of heavy duty mechanised material
handling equipment.
-
Special effort was made by the
consultants for the designing and providing of fabrication details and
intensive technical supervision of the execution of the following:
-
slip-form work for 6 columns,
supporting the bottom slab of the 22.4 m dia. blending silo, simultaneously,
along with the outer silo shell up to + 23.5 m level and thereafter the
lifting of heavy roof girders along with the slip-form assembly from 23.5
m to 80 m level for their faster erection. By this technique around 41/2
months construction time was saved.
-
slip-form for complete structure
involving column and beam elements for supporting the kiln/raw mill ESP
up to a height of 34 m. The slip-form assembly was specifically designed
to suit the requirements of completing this structure in a short time so
that the erection and commissioning of the ESP can match the commissioning
schedule of the plant. With this new technique, the slip-form work was
completed within 43 days. It would have taken around 140 days with conventional
methods, thus saving over 3 months.
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8.)
Equipment fabrication and erection
The fabrication and machinery
erection quantities involved in the execution of Unit 2 are of the following
order:
-
Steel fabrication: 5000 t
-
Machinery fabrication: 1000
t
-
Machinery erection: 8000 t
-
Insulation work: 14 000 m²
-
Refractory: 3000 t
Some of the factors enabling
fast execution were:
-
About 15 contractors were employed
for fabrication/ erection work supported by JIL's own staff and machinery.
-
A fabrication workshop was developed
on site with adequate machinery (including around 150 welding machines)
and handling facilities. To save time of transport, the following equipment/components
were taken on subcontract by JRC from the main supplier to be fabricated
on site (besides the ducts/chutes and normal fabrication):
-
Tertiary air duct
-
Preheater cyclones
-
Gas conditioning towers
-
Fine coal bins
-
Feed bin (cement) for packer
-
Maintenance cranes were
procured and installed in their respective buildings, which facilitated
smooth and faster
erection especially in the raw and coal mills.
-
For the first time, on JIL's
request, the consultants designed a tailormade crane for lifting and erecting
the grinding table of the Loesche raw mill, with a lifting capacity of
130 t. Use of available built-up girders and sections was made to reduce
fabrication time of the crane on site. With the help of this crane the
grinding table (5 m dia, 130 t weight) was erected in position in less
than one day, instead of 8 to 10 weeks as envisaged originally. This has
greatly helped in reducing the critical path for timely project completion.
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Raw mill/kiln
ESP supporting structure
(constructed
by slipform technique)
| 9.)
Project cost
The original project cost
estimate as approved in May, 1988 was Rs.1340 million. It was once again
reviewed after most of the orders had been finalised and the project was
at an advanced stage, in August 1990. This updated figure totalled Rs.1740
million. Thus, the specific investment per annual tonne of installed cost
works out at Rs.1450 which would probably be one of the lowest considering
that the specific investment costs of green field projects in India today
is in the range of Rs.3000 to 3500 per annual tonne.
Out of the total project
cost, the import content was only of the order of Rs.127 million, in terms
of foreign exchange requirements, which amounts to only about 7.3% of the
total project cost. The imports were restricted to the following items
of equipment:
-
Critical components for blending
silo and kiln feed equipment,
clinkerisation unit and ESP's from F.L. Smidth, Denmark.
-
Critical components for vertical
roller mills from
-
Loesche, Germany.
-
Gearboxes for vertical roller
mills and cement mill-3 from
Maag, Switzerland.
-
Bulk Material Analyser (PNAA)
from Gamma Metrics, USA.
-
Critical components for stacker
reclaimers and split sampler
from MVT, Germany.
-
Air lift pumps in clinkerisation
unit from Claudius Peters,
Germany (through F.L.Smidth).
-
Clinker conveyor (pan type)
from Aumund, Germany (through
F.L.Smidth).
-
Critical parts of Cement Mill-3
from Fuller, USA.
-
Torsion shafts for Cement Mills
1 & 2 modifications from
A.Friedr Flender AG, Germany.
-
Rotor assembly for raw mill
ESP fan from TLT, Germany (through Loesche).
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10.)
Project management implementation
The overall responsibility
for project management was with the owner. However, a predominent role
was played by the Consultants (Holtec and HMC) with regard to coordination,
supervision and advice to the owner in respect of multifaceted contracts
and technical decisions involving numerous suppliers and contractors.
Important stages concerning
the implementation of this project are enumerated below:
-
Appointment of consultants
July, 1988 (Holtec
& HMC)
-
Issue of main machinery tenders
October, 1988
-
Order placement for main machinery
April/May, 1989
-
Start of civil construction
July, 1989
-
Start of mechanical erection
March, 1990
-
Start of trial runs February,
1991
-
Commissioning of clinkerisation
and cement mill modification
April, 1991
The delivery of Cement Mill-3
was unduly delayed due to a long-drawn force majeure at the manufacturer's
works. It has since been received on site in October 1991 and is expected
to be commissioned at the time of going to press.
A constructive and co-operative
working environment was established between the owner, its consultants,
suppliers and contractors. A flexible attitude from all concerned, coupled
with sensible management policy contributed toward the swift progress of
the project. This was achieved despite unforeseen difficulties and constraints,
in particular the Gulf War!
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| 11.) Conclusion
Just after 1986, when JIL
had commissioned their first million tonne cement plant, the cement industry
in India was passing through a period of glut. Most of the cement plants
were struggling to keep themselves afloat in the changing environment of
the free-market and glut situation. However, in mid-1987, JIL considered
doubling their capacity at the same premises. Despite apprehension from
various quarters, JIL showed tremendous confidence in the future of India's
cement industry.
The company's experience,
both in the construction and the management of its first project, has proved
useful in the speedy commissioning of its 2nd unit. The company is already
considering further expansion plans, for which feasibility studies are
under way.
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