experience of “the india cements ltd” · requirement of huge investment for building...
TRANSCRIPT
Alternate fuel Usage
Experience of “The India
Cements Ltd” By
D.Sivagurunathan The India Cements Ltd
1.6 2.8
4.0
6.8 7.0
8.8
1989 - 1990 1990 - 1997 1997 - 1998 1998 - 1999 1999 - 2001 2001 - 2005 2005-2010 2011
Experienced cement player with over six decades in business. One of the largest cement
group with a capacity of 16mtpa cement production. Largest manufacturer in South
India with 20% market share. Capacity scaled up 10 times
since 1990 primarily through acquisitions and upgradation.
Brief Overview
Growth history
Chilamkur acquisition
New 1mtpa plant at Dalavoi . Yerraguntla acquisition
New 1mtpa plant at
Malkapur.
Addition of Malkapur-II,
Chennai, Parli &
Upgradation of other plants
Raasi acquisition
Dalavoi 1.3mt
Sankaridurg 0.7mt
Raasi 2.3mt
Malkapur 2.2mt
Chilamkur 1.3mt
Yearraguntla 0.5mt
Sankarnagar 1.6mt
Andhra Pradesh
Tamil Nadu
Kerala
Karnataka
The India Cements Ltd Company Snapshot
15 16
New 1MTPA plant near Banswara, Raj
Non-recyclable Plastic Wastes
as Alternate Fuel
Generation of Plastic Waste in India
Generation of MSW : 1,20,000 tons per day (TPD)
Generation of Plastic Waste : 10,000 tons per day (TPD)
(9% of MSW)
Recyclable plastic : 80% of the total plastic waste
(Taken care by rag pickers)
Non-Recyclable plastic : 20% of the total plastic waste (Matter of concern)
Municipal Waste Combination
WASTE MATERIAL AVERAGE %
PLASTIC 9%
GLASS 11%
METAL 3%
PAPER 13%
BIO DEGRADABLE 55%
INERTS 9%
TOTAL 100%
Environmental Hazards of Plastic Waste Very thin Plastics carry bags, laminated pouches (including Gutka pouches)
and other non-recyclable plastics are littered in tourist places, near ancient monuments and spoil the aesthetic view.
Plastic bags are non-biodegradable and its disposal may make land in-fertile due to impervious nature, choke the open drains and cause death of cattles on ingestion.
Littered plastics spoil beauty of the city and make many important public places filthy.
Garbage containing plastics when burnt in open may cause air pollution problem and particularly burning of plastics may emit obnoxious gases.
Garbage mixed with plastics interferes in processing municipal solid wastes into fertilizers and also causes problems in landfill operations.
Need for safe disposal of plastic waste At present the Non-Recyclable Plastics are disposed to some extent by
open yard burning.
Major portion remains on the soil, which affect the Nature in many forms.
Burning plastic waste in cement plant kiln is the best proven scientific method.
Tamilnadu pollution control board (TNPCB) has initiated action for safe disposal of non-recyclable plastic wastes in cement kilns.
Progress on the usage of Plastic waste Total non-recyclable plastic waste generation in Tamil Nadu
is about 750 Tons/Day.
Tamilnadu has been divided into 7 zones for collection of non-recyclable plastic wastes and each zone is assigned to one cement plant for burning the same.
A work shop was conducted by TNPCB on the usage of plastic waste on 26.08.2009
Trial run of co-processing of plastic waste was started at ICL sankarnagar on 25.10.2009.
Progress on the usage of Plastic waste MoU Signed between ICL and Zone-1 Municipal
corporations on 08.02.2010 for supply of plastic wastes.
Plastic shredders were commissioned in the first week of July 2010.
Originally the plastic fluff was fired in the precalciner with other bio-fuels. Mixing fluff with other fuels was posing problem.
However it was found much easier to pump plastic fluff into the kiln burner from shredder directly. This avoids storage and re-handling of fluff.
Sl. No
Name of the Municipality
Generation of
non -recyclable
plastic T/day
Avg. receipt of
non- recyclable
plastic T/day
Avg.
receipts in %
Gap in %
1 Tirunelveli Corporation
1.80 0.16 10.00 90.87
2. Tuticorin Corporation
2.28
0.07
3.05
96.95 3. Tiruchendur Town Panchayat
4. Nagercoil Municipality
1.66
0.13
7.80
92.02
5. Kanyakumari
Total 5.74 0.36 6.27 93.73
Waste Generation / Usage Summary
Problems in usage of plastic waste Poor collection of non-recyclable plastics from garbage at source.
The gap in collection is more than 90% which means there is high potential in this project if efficiency of collection is improved.
Absence of any regulation for compulsory segregation of plastics at source.
Reluctance of Municipal corporations to segregate at garbage dumps due to financial constraints.
Fool-proof elimination of foreign materials from the plastic waste.
Mechanization of plastic waste feeding to the shredder.
Constant feeding of shredded plastic waste into the kiln with controls.
High investment with uneconomical return is major deterent for progress further. Any investment from developed countries would help expansion of this project
Industrial wastes as alternate fuels
Specification of HW for use of energy recovery (CPCB Guideline – Feb 2010)
Parameter Limit
Calorific Value As received basis >2500 k Cal/ Kg Ash
Liquid Solid
<5% <20%
Chloride <1.5% Halogens ( F+Br+I) <1.0%
Sulphur <1.5% PCB/PCT( ppm) <5.0
Heavy Metals (ppm) Hg
Cd+TI+Hg
<10 <100
pH 4 to 12
Viscosity (cSt) for Liquid < 100 Flash point ( Deg centigrade) ( for Liquid) <60
Specification of HW for use as Alternative Raw Material (CPCB Guideline-Feb 2010)
Parameter Limit
Volatile organic Hydrocarbon < 5000 ppm
Total organic carbon (TOC) <1000 ppm
Cao+SiO2+Al2O3+Fe2O3+SO3 (In Ash) >80%
Chloride <1.5%
Sulphur <1.5%
PCB/PCT( ppm) <5.0
Heavy Metals (ppm) Hg Cd+TI+Hg
As+Co+Ni+Se+Te+Sb+Cr+Sn+Pb+V
<10
<100 <10,000
Potential Waste Generators
Pharmaceuticals Chemicals Paint/coating manufacturers Petrochemicals Printing Ink Manufacturers Printing Companies Automobile Manufacturers Solvent Recyclers Waste disposal Brokers
Typical Chemical Families That make up the liquid Fuels
Aromatic Hydrocarbons Aliphatic Hydrocarbons Alcohols Acetones Acetates Ketones Esters Glycols Chlorinated Hydrocarbons Oxygenated Hydrocarbons
Industrial wastes used in ICL plants Spent carbon, from Pharma Industry as partial fuel replacement (Kiln
Burner) Organic liquid waste from Pharma Industry as partial fuel replacement
(Kiln Burner) Polymer sludge from Chemical/Paint Industry)- (Fed to Calciner)
Spent Carbon Proximate Analysis
Free Moisture % 24.4
Inherent Moisture % 3.48
Volatile Matter % 12.4
Fixed Carbon % 42.72
Ash % 40.4
Gross C.V. K.Cal/Kg % 4108
SO3 % 0.32
Name DMF (Liquid)
NON Sterilize Residue
IPA Residue
MDC Residue
Mixed Residue
IPE + ED
Residue Inherent Moisture % 92.23 3.35 10.56 5.26 6.32 4.92
Volatile Matter % 7.32 93.69 84.35 93.41 65 64.74
Fixed Carbon % 0.31 0.88 3.79 0.60 0.53 17.7
Ash % 0.14 2.08 1.30 0.73 28.15 12.64
Gross C.V. K.Cal/Kg 5475 7337 7904 7421 4511 4963
Proximate Analysis of various wastes from a typical Pharma Industry (both solid & liquid)
Properties of Polymer cake /sludge from Chemical/Paint Industry
S.no Test parameters Result Units
1 Bulk Density 0.5612 gm/ml
2 Flash point 95 %
3 Calorific value 6519 Cal/ gm
5 Loss on Drying 21.9 %
6 Loss on Ignition 98.81 %
7 Chlorides 601 mg/ Kg
8 Sulphates 433 mg/Kg
9 %organic content 3.7 %
10 Hexavalent chromium BDL mg/Kg
11 Nickel BDL mg/Kg
12 Zinc BDL mg/Kg
13 Copper BDL mg/Kg
14 Manganese BDL mg/Kg
15 Cyanide BDL mg/Kg
16 Lead <1 PPb
17 Mercury 11 PPb
Impediments in usage of Industrial wastes Absence of statutory law that polluters pay. Polluters sell their waste at high
price or adopts improper disposal method.
Long Wait for Clearances from Statutory Bodies.
Inconsistent availability of waste.
Competition from others in cement industry.
Requirement of huge investment for building infrastructure to handle, store and use industrial wastes along with conventional fuel.
Strong odour which invites protest from public as well as employees.
Problem of Transportation of hazardous wastes in view of high inflammability.
Bio-fuels
Agricultural wastes as renewable bio-fuel
Cashew shell is major bio-fuel. It has very good heat value. The other bio-fuels are rice husk, ground-nut shell, coconut shell, chilli stems, etc.
No processing is needed. Easy to regulate the feed into the kiln.
No adverse smell or health hazard but high volume storage and handling is posing problem
Availability of bio-fuel is erratic and seasonal. Since agriculture is small scale and scattered, procurement of sizable quantity is problem
The cost is high since it is used as fuel in village homes and small scale industries
Fuel GCV Cal/gm
NCV Cal/gm Moisture C H N S ASH O
Saw dust 3952 3798 10.81 43.65 5.83 0.52 0.11 2.05 47.84 Rice Straw 3382 3228 11.01 38.69 5.78 0.59 0.11 14.54 40.29 Ground Nut shell 4091 3937 10.4 44.55 6.02 0.02 0.09 5.16 44.16 Bamboo dust 4127 3973 9.9 46.89 6.77 0.34 0.1 2.09 43.81 Bagasse 4172 4018 8.38 46.73 6.24 0.44 0.01 3.49 43.09 Cane Trash 4032 3878 10.33 43.76 6.19 0.93 0.1 5.91 43.11 Rice husk 4067 3912 12.24 34.52 5.55 1.35 0.15 24.34 34.09 Wheat Straw 3980 3826 7.96 40.21 5.08 0.61 0.11 7.04 46.95 Coir Waste 4312 4158 7.86 45.16 5.26 0.2 0.18 2.14 47.06 Padak Dust 4724 4569 9.81 43.05 5.76 0.4 0.05 0.62 50.12
Calorific Value of Bio- Mass Fuels
Wood Chip as renewable bio-fuel
1. Wild shrub called JULI FLORA which grows uncontrolled in barren uncultivable land offers excellent scope for bio-fuel.
2. Even after trimming the plant up to the root, it grows from root very fast. It grows through out the year.
3. Availability of large barren land and wild growth of Juli-flora in it is abundant. There are many thermal power plants operating on exclusively Juli-flora woodchips as fuel.
4. Absence of viable mechanization for harvesting Juli-flora is problem. The cost of manual harvesting is high.
Wood Chips of Juli-flora plant
Wood Chipper
C3S Size C2S Size % C3S % C2S Liquid%
Normal Clinker
18.0µ 9.9µ 50.6 33.2 15.2
AFR Clinker
18.7
10.5
49.5
34
16.0
Microstructure of Normal Clinker Vs. 5-8% AFR clinker
Similar microstructure except marginal increase in crystal size & liquid content in AFR clinker
Chemical Characteristics of Clinker with use of Spent carbon/sludge
Oxide composition
Clinker-1 (Normal)
Clinker-2 (With AF) Phase
Composition
Clinker-1 (Normal)
Clinker-2 (With AF)
SiO2(%) 21.0 20.7 Bogue Potential Phase
Al2O3(%) 5.6 5.80 C3S(%) 53.4 53.2 Fe2O3(%) 4.65 4.40 C2S(%) 19.9 19.3 CaO(%) 65.1 64.9 C3A(%) 7.1 8.0 MgO(%) 1.05 0.95 C4AF(%) 14.2 13.7 SO3(%) 0.30 0.35 Chemical Parameters
Na2O(%) 0.38 0.55 Liquid Content (%) 28.6 29.0
K2O(%) 0.44 0.61 AM(%) 1.21 1.29 Cl (%) 0.004 0.008 SM(%) 2.04 2.03 F- (%) 0.01 0.03 LSF(%) 0.95 0.94
Mn2O3 (%) 0.05 0.05 F.CaO(%) 1.65 1.80
P2O5 (%) TiO2
0.18 0.15
0.21 0.22
Except marginal increase in Alkalies and minor elements , no difference in chemical/ phase composition observed.
Influence on Clinker Quality Alternative Fuels Such as Plastic fraction potentially contain
minor traces of metals Contents Given in mg/kg if not specifically mentioned
Petcoke Plastic Waste Oil Prepared Domestic Waste
Cd 0.005 2-8 13 3.3
Cl 25 12800 8400 1.23
Cr 1 9 7.6
Hg 0.2 0.3 2 0.15
Ti 0.2
Zn 5 114-177 3000 378
Conclusion
Co-processing of waste derived materials (both hazardous & innocuous) in Cement Kiln is a sound method of safe disposal of and benefits the Environment.
It has been proven that heavy metal elements are safely captured in
clinker phases and the high thermal profile in the kiln ensures cracking of the hazrdous organic compounds of the WDF down to its base molecule methane (CH4) and then is completely combusted. The clinker quality does not suffer on account of WDF usage.
The competitiveness of the cement industry in the near future will
be decided by the extent of Substitution of primary fossil fuels with alternate fuels.
Thank you
Littering of Plastic wastes
Plastic wastes spoil city’s beauty
Plastics choke water bodies
Burning of plastics
Burning plastic wastes in open
Plastic shredder in operation
Shredded Plastic Fluff
Shredding & Feeding of Plastic Waste Directly into the kiln burner
Shredding & Feeding of Plastic Waste Directly into the kiln burner
Coconut Shell