Steel demand projections
India
has become the 3rd largest steel producer in the world with a production of 91
MT and a capacity of 125 MT in FY 2015-16. The low per capita steel consumption
of being low at 61 Kg in India compared to world average of 208 Kg, there is
significant potential for growth. As per the National Steel Policy, 2017, the
crude steel demand will grow threefold in next 15 years to reach a demand of
255 MT by 2030-31. It is anticipated that a crude steel capacity of 300 MTPA
will be required by 2030- 31, based on the demand projections. Even with this
demand of crude steel by 2030-31, India’s per capita finished steel consumption
would reach only to 158 Kg. However,
achieving crude steel capacity up to 300 MT will require extensive mobilization
of natural resources, finances, manpower and infrastructure including land.
Requirement of
coking coal
As
per the aforesaid Policy, the demand for coking coal is expected to be 161 MTPA;
that of non-coking coal for PCI about 31 MTPA and the non-coking coal
requirement for DRI route is estimated at 105 MTPA by the FY 2030-31.
The
current dependence on imported coal is about 85%, which as per the National
Steel Policy is supposed to be brought down to 65% by 2030-31. This indicates
that 35% of the total requirement of 161 MTPA by 2030-31, i.e., 56.35 MTPA
needs to be met from the domestic sources by the year 2030-31. This is a great
challenge for both the Steel Producers and the Coal Producers in the country.
The
National Steel Policy aims at increasing the availability of coking coal
through overseas asset acquisition, establishing sufficient number of modern coking coal
Washeries, facilitating allocation of indigenous coking coal reserves in the
country exclusively to steel sector with no diversion of such coal to any other
sector, facilitating exploration and optimal utilization of deep seated coking
coal reserves, expeditious
implementation of Jharia Action Plan to improve the domestic availability of
coking coal and taking suitable fiscal
measures to support the rising requirement in the steel sector.
Coking Coal
Availability in India
Though,
India is fortunate to have 3rd largest share of coal resource in the
world, the quantity of coking coal is very limited. Further, due to the “Drift
Theory” origin of coal in India, where the woody material was transported to
longer distances, carrying along external impurities, made such coals contain
very high amount of inert material or mineral matter, commonly known as ash
content. These mineral matters are finely disseminated within the coal matrix,
which have made the coal more difficult to be washed or beneficiated for
reducing the ash content.
Coking
coals in India are categorised in three categories, namely Prime Coking Coal,
that can form coke for metallurgical purposes without blending with other
coals: Medium Coking Coals, that require blending with Prime coking coals for
coke making: and Semi-coking Coals that are weak in coking properties but can
be blended in small proportions with Prime coking coals for coke making.
Prime
coking coals are available in India only in the upper seams (Seams IX and
above) of the Jharia Coalfield, which have mostly been exploited in the past
and the remnant resources are now available in the surface constrained areas
like, Surface Fires, Rivers, Townships, Human Settlements and Road & Rail
infrastructures.
Medium
coking coals are available in various coalfields in Jharkhand (lower seams of
Jharia coalfield, Raniganj, East Bokaro, West Bokaro, Ramgarh, North Karanpura
& South Karanpura), West Bengal (Raniganj coalfiled) and, Madhya Pradesh
(Pench Kanhan & Sohagpur), which have substantial resources with high ash
content.
Semi-coking
coals are available in very limited areas of West Bengal (Raniganj coalfield),
Jharkhand (Ramgarh coalfield and Chhattisgarh (Sonhat coalfield).
As
per the GSI estimates of 2017, the total coking coal resource in India is 34.533
billion tonnes (Bt) with Prime, medium and Semi-coking being 5.313Bt, 27.512Bt
and 1.707Bt respectively. Based on the status of exploration the break-up of
these resources is as follows1:
Coal
Type
|
Measured
Resource (billion tonnes)
|
Indicated
Resource (billion tonnes)
|
Inferred
Resource (billion tonnes)
|
Total
Resource (billion tonnes)
|
Prime
Coking
|
4.614
|
0.698
|
0.000
|
5.313
|
Medium
Coking
|
13.500
|
12.132
|
1.879
|
27.513
|
Semi-coking
|
0.519
|
0.995
|
0.193
|
1.707
|
Total Coking
|
18.634
|
13.826
|
2.072
|
34.533
|
1. Source GSI publication
General characteristics
of coking coal
Coking
coals are such coals that can form quality coke during carbonisation. Coke
quality in terms of cold and hot strength plays an important role in the smooth
running of Blast Furnaces. The four most important characteristics of coke that
dictate the right quality parameters of coking coals required to make such coke
are, Micom-10, Micom-40, CSR and CRI values. These are basically the strength
parameters of the coke at different conditions.
Amongst
all ranks of coal, depending on their age (Peat, Lignite, Bituminous and
Anthracite), only a few bituminous coals possess the required properties for
production of right quality coke for the use in a Blast Furnace. As such, the
quality parameters of the coking coals are very important for deciding the
blend ratio of different coking coals from different sources for making a good
coke. The required characteristics of coke are achieved by making coke after
blending coking coals from different sources to satisfy the pre-defined
proximate characteristics, ultimate analysis characteristics rheological
properties, petrographic properties and the ash chemistry.
Important
parameters of the proximate analysis are the moisture content, volatile matter
and the ash (inorganic residue), each expressed as percentage of total. The
ultimate analysis results show the percentages of different elements like C, H,
N, S and P.
In
the rheological properties, Free Swelling Index (FSI) or Crucible Swelling
Number (CSN), Maximum Fluidity (ddpm) and Plastic Range are very important to
decide the suitability of any coal for coke making. For high strength coke,
various coals used in the blend should have a broad range of common plastic temperature;
otherwise coals will not be compatible.
During
the process of formation of coal, that is, conversion of wood or plant material
to bituminous coal stage, different types of macerals, like Vitrinite,
Semi-Vitrinite, Liptinite, Exinite and Inertinite are formed that behave
differently upon heating. Only the first four macerals are characterised as
reactives. Petrographic properties are determined through microscopic studies
of coal samples for determination of their type, rank and mineral matter.
General characteristics of coking coals show that the reflectance of Vitrinite
(Ro) varies from 0.6% to 1.8%, however, the acceptable range of reflectance
(Ro) for good coke making varies from 1.1% to 1.4%. Mean maximum reflectance
(MMR), which is denoted as Rmax or MMR is normally 1.066 times Ro value.
The
ash chemistry of coal in terms of its composition as CaO, SiO2, Al2O3,
Na2O, K2O etc. are also important to decide whether the
slag of the Blast Furnace will have acidic nature or basic nature.
Thus,
it can be seen from the above that selecting a particular coal for coke making
requires rigorous testing of the same in terms of the different required
properties and making coke after blending the same with other suitable coals to
meet the required coke parameters.
Quality Comparison
of Indian Coking Coals with Australian coking coal
Australia
is the major supplier of coking coal to India and also to the world trade.
Indian Steel producers meet their requirement of coking coal largely from
Australia and partly from USA, New Zealand, Mozambique, Russia and China.
Quality-wise Australian coals are superior and as such are more favoured by the
Indian Steel industry. However, the international price of coking coal is very
volatile and becomes unaffordable for the steel producers at times.
A
comparison of some typical imported Australian coking coal with typical Indian
coking coals is shown below2:
Sl.
No.
|
Coal/coke
parameters
|
Australian
coking coal
|
Indian
washed coking coal
|
Remarks
|
A
|
Proximate
Analysis
|
|||
Moisture
(%)
|
1
- 2
|
2
– 2.5
|
||
Ash
(%)
|
7.5
- 9.8
|
15.24
– 18.03
|
Higher
in Indian coals.
|
|
Volatile
Matter (%)
|
19.3
- 24.3
|
18.58
– 24.84
|
||
B.
|
Ultimate
Analysis
|
|||
Carbon
(%)
|
88.3
- 90
|
70.9
– 75.1
|
||
Hydrogen
(%)
|
4.67
- 5.0
|
4.03
– 4.23
|
||
Nitrogen
(%)
|
1.8
- 2.06
|
1.08
– 1.57
|
||
Sulphur
(%)
|
0.55
- 0.7
|
0.57
– 0.83
|
||
Phosphorous
(%)
|
0.007
- 0.07
|
0.026
– 0.18
|
||
C.
|
Petrographic
Analysis
|
|||
Vitrinite
(%)
|
55
- 70
|
46.5
– 55.0
|
Lower
in Indian coals.
|
|
Liptinite
(%)
|
0
- 1
|
0
– 4.4
|
||
Exinite
(%)
|
0
|
0
|
||
Inertinite
(%)
|
27
– 42
|
38.1
– 45.6
|
Higher
in Indian coal.
|
|
Mineral
Matter (%)
|
2
– 4
|
5.9
– 9.9
|
Higher
in Indian coal
|
|
Vitrinite
Reflectance (Rmax)
|
1.17
– 1.55
|
0.98
– 1.3
|
Lower
in Indian coal.
|
|
D.
|
Ash
Analysis
|
|||
SiO2
|
50.3
– 66.5
|
8.22
– 11.25
|
||
Al2O3
|
28
– 33.1
|
4.92
– 5.29
|
||
Fe2O3
|
2.4
– 7.6
|
0.01
– 1.05
|
||
CaO
|
0.2
– 3.9
|
0.095
– 0.63
|
||
Na2O
|
0.3
– 0.9
|
0.001
– 0.052
|
||
K2O
|
0.85
– 1.5
|
0.2
– 0.33
|
||
E.
|
Caking
Property
|
|||
CSN
|
7.5
– 9.0
|
5
– 6
|
Lower
swelling index due to higher ash in Indian coal.
|
|
Gray
King Coke Type
|
G5
– G10
|
C
– E/F
|
Relatively
inferior coke type
|
|
F.
|
Giesler
Plastometer Value
|
|||
Maximum
Fluidity (ddpm)
|
75
– 1100
|
772
- 2400
|
Superior
fluidity in Indian coal.
|
|
G.
|
Coke
Properties
|
|||
Micum
M40
|
80
– 84
|
NA
|
||
Micum
M10
|
7
– 8
|
NA
|
||
Coke
reactivity index (CRI)
|
21
– 35
|
NA
|
||
Coke
Strength after reaction (CSR)
|
65
– 72
|
NA
|
2. Source: Compiled from various available sources.
Coking coal price
concern
Historically,
price of imported coking coal had a downward trend since 2012 (US$ 252.1) till
2015 (US$ 90). From the second half of 2016, there has been steep rises in the
prices, sometimes touching the figure of US$ 260 per tonne. Coking coal prices
in the international market continue to trend higher since December 2017 on the
back of supply tightness in Queensland, Australia. Difficulties in securing
loading slots in Queensland for contract cargoes continued to tighten global
supply of coking coal in late 2017. In March 2018 the prices are in the range
of US$ 220-225 per tonne.
Soaring price of internally traded coking coal is a
cause of great concern for the Indian steel producers due to their
competitiveness in the world market for the steel products.
Need for demand
side management
With
the limited availability of domestic coking coal for the required quality and
its spiralling high prices in the international market, it is necessary to look
at the demand management side. It is more so important when we look at the
current consumption rate of coke in Indian Steel Plants vis-Ã -vis global best
practices. The National Steel Policy endeavours to pursue with the Integrated
Steel Plants to reduce their coking coal consumption at par with global best
practices by resorting to auxiliary fuel injection technologies like Pulverized
Coal Injections (PCI)/ Coal Dust Injection (CDI) or natural gas/ syngas
injection along with PCI/ CDI.
Targets
for the techno-economic performance, as set forth in the National Steel Policy
are as shown below:
Parameters
|
Units
|
International
Best Practice
|
Current
|
Target
for 2030-31
|
Coke
Rate
|
Kg/thm
|
275
- 350
|
400
- 600
|
300
– 350
|
CDI
Rate
|
Kg/thm
|
200
– 225
|
50
– 200
|
180
- 200
|
BF
Productivity
|
tonnes/m3
/day
|
2.5
– 3.5
|
1.3
– 2.2
|
2.5
– 3.0
|
Specific
Energy Consumption
|
Gcal/tcs
|
4.5
– 5.0
|
6.2
– 6.7
|
5.0
– 5.5
|
Coking coal
production plan of Coal India Ltd for FY 2019-20
CIL
has planned to enhance its coal production to the tune of 908MT by 2019-20. A
breakup of the planned production vis-a-vis individual subsidiary is as follows3:-
Subsidiary
Name
|
Total
(MTPA)
|
Coking
coal (MTPA)
|
Non-Coking
Coal (MTPA)
|
|
G-10
& superior
|
G-11
& inferior
|
|||
ECL
|
62.0
|
0.25
|
44.75
|
17.0
|
BCCL
|
53.0
|
45.78
|
7.22
|
-
|
CCL
|
133.5
|
24.4
|
45.57
|
63.5
|
NCL
|
110.0
|
-
|
96.00
|
14.0
|
WCL
|
60.0
|
0.52
|
59.48
|
-
|
SECL
|
239.6
|
0.14
|
20.42
|
219.0
|
MCL
|
250.0
|
-
|
1.5
|
248.5
|
Total
|
908.10
|
71.12
|
274.94
|
562.04
|
3. Source: Published paper in the 5th International Conference on
Coal Washing.
As
can be seen from the above, around 71 MT of coking coal is planned to be
produced, but due to non-availability of adequate washing capacity in CIL, most
of these are being supplied to the power plants. This is the current practice
and is likely to continue until the washery construction programme of CIL gains
ground.
Coking coal washing
- Present capacity and future plans
Most
of the coking coals, being produced currently and also projected to be produced
in future, are of inferior grade with ash content generally exceeding 35%. The
current washing capacity of Coal India for coking coals is around 23.3 MTPA and
it has a plan to set up new coking coal washeries to meet the requirement of
coking coal for the steel producers. However, as Indian Coking coals have very
poor washability characteristics these washeries are planned to wash at 18-19%
ash content.
At
present the total installed capacity of the coking coal washeries in India is
about 31 MTPA which operate at around 20-30% capacity utilisation. Such low
capacity utilisation is owing to the fact that most of them were set up 4 to 5
decades ago and not much required improvements were made in them with the
changing quality of feed over the years. These washeries were planned with feed
from superior grade coals, which have since exhausted.
CIL
has identified to set up 18 new coking coal washeries with total throughput
capacity of 48.2 MTPA (Source: Corporate presentation of CIL, April 2017) in
its various subsidiaries under BOM/BOO concept. Three of these washeries at
BCCL with a combined capacity 11.6 MTPA are likely to be commissioned shortly. Other
three coking coal washeries with total capacity of 7.0 MTPA are in different
stages of construction and are likely to commission by the year 2019-20. Additional
one new coking coal washery with throughput capacity of 3.5 MTPA is planned to
be set up at Tasra project of SAIL.
In
view of the above the total installed capacity of the new washeries and the
existing washeries of Tata Steel would be about 59.4 MTPA, which at an average
yield of about 45% - 50% can provide clean coals at 18% ash to the extent of 27
to 30 MTPA. As most of the existing washeries would be replaced with the new
ones, there still remains much gap between the estimated demand of coking coal
from indigenous sources and its likely
availability. Further, it is also important to examine whether, all the
domestic coal with 18-19% ash can be blended with imported coal at the steel
plants from the point of view of Blast Furnace productivity and the related
costs.
Prospect of washing
Indian Coking coal at lower ash level
A
Committee was constituted by the Ministry of Coal, Government of India in March
2017 under the Chairmanship of CMD, CMPDI with members from Steel and coking
coal producing companies, CIMFR and
IIT(ISM), Dhanbad for assessing the technical feasibility of washing coking
coals (W-IV/ LVMC) to 13% ash content and the cost economics thereof.
Comprehensive
studies were made by collecting samples of coking coal from the mines/seam
currently under production, conducting washability tests and evaluating the
cost of clean coal at 18% ash, 15% ash and 13% ash. The Committee’s major findings
were as follows:
- In general, the desired selling price of clean coal produced on washing W-IV coal is less than the desired selling price of clean coal produced on washing ungraded coal.
- In the case of washing coal to obtain cleans coal at 13% ash, there is huge generation of middlings as compared to that at 18% ash clean coal. Marketability of such huge quantity of middlings needs to be looked into.
- In the case of clean coal at 13% ash, it is obvious that significant quantity of coal having coking properties is reporting to the middlings which could otherwise be used for metallurgical purpose.
- Depending on the quality of raw coal feed (W-IV & ungraded) and its washability characteristics, the theoretical yield of clean coal at 13% ash varies from 13% to 28% and the corresponding middlings at 34% ash varies from 62% to 51%, which is more than double the quantity of middlings generated at 18% ash clean coal. This indicates that huge quantity of coal having metallurgical properties migrates to middlings which can otherwise be used for metallurgical purpose if washed to obtain clean coal at 18% ash level.
- For washing W-II/ W-III grade coking coal at 13% ash clean coal, new washeries may be set up in the areas where there is potential of better yield leading to favourable techno-economics and the consumer is willing to accept clean coal at that price on long-term basis.
- The technology for Washing may be selected on the basis of percentage of Near Gravity Material (NGM) at the cut-off ash, which could be Jig for <20% NGM and Heavy Media for >20% NGM.
- Washing of coking coal to produce clean coal at 13%, 15% and 18% may be considered based on the overall economics of the project which is greatly dependent on yield%. To have a balance between cost of production, yield and ash%, project specific study needs to be carried out in a holistic manner.
- In view of the above, it was recommended that washing of coking coal (WIV & LVMC) at 18% ash level will give viable techno-economics for both Steel Sector and CIL.
Emerging Technologies
for extracting less than 10%-12% ash coal from high ash Indian coking coals.
A. Studies done by CIMFR
CIMFR had conducted some studies
on grinding of Low Volatile Coking coal to 100 micron size and then
beneficiating it by floatation. To achieve the low ash (below 12% ash content,
two-stage floatation studies were carried out. The typical results of the
rougher and cleaning stage floatation by floatation column is shown in the flow
sheet.
This
coal has potential to give the product around 10%-12% ash content with 41%-42%
yield and second product can be produced around 34%-35% ash having 16%-17%
yield. The overall yield in two stage processes is around 57%-58%. The rejected
tailings are having 68% ash content. The
second product can be used directly for power generation. There is also the
possibility by blending the tailings with product II to use in fluidized bed
power generation plant to utilize the full combustible values.
This study indicates that
there is ample potential to get up to 10% ash coking coal from Indian ROM
coking coals. However, its cost economics and the technology for binding the
100 micron size product, to make them transportable, needs to be developed.
It is
suggested that Indian Steel Producers should commission Research Organisations
to develop this technology to recover maximum carbon from the domestic coking
coal. It may be worth mentioning that the technology for drying and
conditioning micron size coals to form a product in pellet size has already
been developed in USA, which would require to be adopted in this technology.
B Recent developments in coal refining (reducing
ash in clean coal to around 5%)
A remarkable new coal technology
has been developed recently in the USA where coal refuse from the coal
washeries are processed to efficiently separate it into hydrocarbon, mineral
matter and water factions. The process takes place at a very small particle
size (averaging around 100 microns) enabling the particles to respond to nano
agents – the coal becomes very hydrophobic, facilitating very effective
ash-mineral separation. The hydrocarbon fuel separated from this process is an
extremely high quality coal and is produced as a robust, stable pellet with
approximately 2 % moisture and 5% ash. As a fuel, such low ash-low moisture
hydrocarbon fuel delivers substantial value in use for power stations (for
thermal coal) and steel production (for coking coal).
Pilot scale demonstration of such
separation at a capacity of 3 tph module has been made with the result of
substantial reduction in the ash content and improvement in the FSI of coking
coal rejects. It is also gathered that a number of small modules of 3 tph could
be clubbed together to create an integrated capacity of 2 MTPA throughput for
such processes.
Though, the above mentioned
development is quite new and requires to be evaluated on commercial scale, the
development itself appears to be innovative and requires a closer scrutiny for
its use on a commercial scale for treating Indian coking coals which have
inherently high ash content.
Conclusions
Indian
Steel Producers are facing a lot of challenges in meeting the competitiveness
of marketing steel in the world market due to highly volatile prices of coking
coal. This is further compounded by the mammoth plan of increasing steel
production in India in the coming 15 years. Domestic coking coal, having high
ash content and difficult to wash characteristics, restrict their washability
at lower ash levels and become extremely costly compared to the internally
traded coking coals. However, in order to control overall costs of production
of steel, it is necessary to blend domestic coking coals to the maximum extent,
without compromising on the overall cost of production of steel. A lot of
R&D work has to be undertaken to harness maximum quantity of coal at lower
ash from the domestic coal. The conventional system of gravity based coal
washing is not a solution to the increasing demand of coking coal. The emerging
technologies need to be developed as discussed in the previous paragraph need
to be tried and established to make them commercially viable to increase the
availability of domestic coking coal for metallurgical purposes. The best way
to maximise utilisation of Indian coking coal would be to conventionally wash
it at 18% ash and treat the rest of coal (middlings and rejects) in the new
technologies to reduce the ash to below 8-10% and blend it with 18% ash clean
coal to reduce the overall ash content of the blend.