Thursday, 15 December 2011

Factors affecting Fuel Rate


1.Gas Utilization   
2.Hot Blast Temperature 
3.Sinter %  
4.Steam Enrichment  
5.Heat loss 
6.Flux Rate  
7.Coke ash  
8.Coal ash
9.Coal RR
10.Slag Rate
11.Fines carryover
12.Metalloids Mn, Ti, P, Si
Fe in Burden

What happens to Fuel carbon in BF?


Input fuel
Coke + Nut  420 kg/thm (from top)
Coal  120 kg/thm (through tuyeres)
»102 kg/thm coke equivalent
Total coke equivalent 522 kg/thm

Out put
In HM as carburization 4.5% say  52 kg/thm coke equivalent

Remaining 470 kg/thm will be used in direct reduction and will burn in front of tuyeres.

Now assume 30% DR
The coke used in DR = 141 kg/thm
Remaining 329 kg/thm will be burnt in front of tuyeres
Out of which coal 120 kg/thm = 102 kg coke equivalent
And the coke burnt in front of tuyeres = 227 kg/thm

Friday, 19 August 2011

Gas Cleaning Systems in Ironmaking Blast Furnaces


In a blast furnace, iron ore and coke are charged into the top of the furnace. The molten iron is removed near the bottom of the
furnace. Combustion air is supplied through tuyeres at a level just above the iron tap hole. The combustion air is called wind. Wind is
air that has been preheated, compressed and may contain added oxygen, natural gas, pulverized coal or other additives. One of the
limiting factors of increasing production of an ironmaking blast furnace is the velocity of the wind in the furnace. If the wind
velocities become too high, the normal downward flow of the charge materials is inhibited.1 One technique used to increase the
amount of wind available for combustion is to increase the pressure at the top of the furnace. This increase in top pressure increases
the pressure of the incoming wind, which increases the gas density, and lowers the wind velocity. Because of the resulting
improvement in blast furnace performance, top pressures above 15 psig are becoming more common and some furnaces are operating
at top pressures as high as 30 psig. 2,3
Blast furnace gas has a modest heating value from the carbon monoxide and hydrogen that it contains. The gas is burned to recover
this heat and to reduce the carbon dioxide emissions from the process. Some of the gas is used to preheat the blast furnace wind in
stoves that are normally located adjacent to the furnace. For efficient operation and longevity of the stoves, the blast furnace gas must
be clean and dry.

Gas Cleaning Systems in Ironmaking Blast Furnaces

1.Venturi.Gas cleaning,
2.Scrubber, 
3.Cyclone, 
4.Dust catcher, 
5.Recovery turbine

Thursday, 18 August 2011

Reasons for Frequent tuyreburning

1] Enlargement of Dead Man Zone

2] Poor hearth Annulus

3] prolonged operation in low blast

4] Insufficient cooling water pressure at tuyre

5] Coke value CRI CSR

6] Manufaturing Defect in tuyre.

7] Viscosity of the slag

8] High Pressure drop in furnace

Tuesday, 16 August 2011

Why the Blast Furnace can be used to extract iron from Fe2O3 but not Aluminium from Al2O3.?

Iron is liberated from it's oxide in a blast furnace by carbon monoxide, the carbon monoxide simply removes oxygen from the iron oxide to become carbon dioxideleaving elemental iron. The same process will not work with aluminum oxide because aluminum has a much higher electropositive potential than iron. What this means in simple language is that aluminum gives up more energy than iron when it forms it's oxide and it takes more energy to remove oxygen from aluminum oxides than it does from iron oxides.

Effect of high Al2O3 slag on the blast furnace operations

Increasing the Al2O3 content in the blast furnace slag, the blast furnace operations tend to make troubles such as excess accumulation of molten slag in the blast furnace hearth and increasing pressure drop at the lower part of the blast furnace. So, it will be important to keep good slag fluidity at the blast furnace operations such as, drainage of tapping and keeping good permeability. In order to clarify the effect of high Al2O3 slag fluidity on the blast furnace, high Al2O3 slag (20%) test operations of experimental blast furnace have been carried out. Investigation results of the test operation are as follows; 1) Slag MgO improves the hearth drainage rate at high Al2O3 slag operation. 2) Permeability of the dripping zone is improved by decreasing slag CaO/SiO2, at high Al2O3 slag operation of the blast furnace. 3) It was verified that the slag drainage phenomena were able to described by the fluid model. 4) The optimum composition of high Al2O3 slag of the blast furnace is high MgO and low CaO/SiO2.

Blast Furnace Slag


Blast Furnace Slag is formed when iron ore or iron pellets, coke and a flux (either limestone or dolomite) are melted together in a blast furnace. When the metallurgical smelting process is complete, the lime in the flux has been chemically combined with the aluminates and silicates of the ore and coke ash to form a non-metallic product called blast furnace slag. During the period of cooling and hardening from its molten state, BF slag can be cooled in several ways to form any of several types of BF slag products.
Blast Furnace: Combustion material and ore are supplied from the top while an air flow is supplied from the bottom of the chamber. This forces the chemical reaction to take place throughout the ore, not only at the surface.

Granulated SlagGranulated slag is rapidly cooled by large quantities of water to produce a sand-like granule that is primarily ground into a cement commonly known as GGBS (Ground Granulated Blast FurnaceSlag), or Type S slag cement. It is also mixed with Portland cement clinker to make a blended Type 1S cement.


Air-cooled Slag,
Blast furnace slag is allowed to slowly cool by ambient air, is processed through a screening and crushing plant and is processed into many sizes for use primarily as a construction aggregate. Common uses are as aggregates in ready-mix concrete, precast concrete, hot mix asphalt aggregate, septic drain fields and pipe backfill.



Pelletized or Expanded Slag
Pelletized or Expanded Slag is quickly cooled using water or steam to produce a lightweight aggregate that can be used for high fire-rated concrete masonry and lightweight fill applications over marginal soils. Due to its reduced weight, it is perfectly suited for aggregate in lightweight concrete masonry, lightweight ready-mix concrete and lightweight precast concrete



Air-cooled Blast Furnace Slag
This smaller sized aggregate is primarily used in chip and seal applications, also known as "Chip Seal" or "Aggregate Seal Coating", applied to existing pavement surfaces. The primary purpose for Chip and Seal is to achieve a skid resistance on rural pavements and to maximize driving safety. It is also used in concrete masonry and hot mix asphalt.





Air cooled blast furnace slag rip rapThe largest slag aggregate, riprap is a permanent cover of rock used to stabilize shorelines and streambanks, and prevent erosion along slopes and embankments. It is also used in gabion baskets, Mineral Wool manufacture (insulation), and lightweight fil


Slag cement,
Slag cement is commonly found in ready-mix concrete, precast concrete, masonry, soil cement, concrete wallboard, floor leveling compounds and high temperature resistant building products. Its measurable benefits in concrete include improved workability and finishability, high compressive and flexural strengths, and resistance to aggressive chemicals

IMAGE BLAST FURNACE


BLAST FURNACE TOP VIEW FROM TUYERE LEVEL IMAGE


Monday, 15 August 2011

Blast furnace operation-flow diagram

Blast furnace burden softening and melting phenomena: Pellet bulk interaction observation

The cohesive zone in the blast furnace, where ferrous burden materials soften and melt, greatly affects the furnace’s performance. Minimizing the size and lowering the position of the cohesive zone will improve productivity and decrease the coke rate. This work was designed to better understand the softening and melting phenomena of ferrous feed materials. Different experimental techniques were used to allow the observation of different stages of softening and melting. This article examines the interaction between pellets at high temperatures under load. The pellets were reduced to 60 or 80 pct reduction degree (oxide basis), placed in a graphite crucible, and heated under N2 gas flow, while X-ray pictures were taken at regular intervals. In addition, the contractions of the pellets and temperature were recorded. These experiments were performed with individual pellet types as well as with a mixed burden of fluxed with acid pellets at a ratio of 2:1. The dripping of liquid from the pellets occurred at different conditions depending on different reduction degrees. In those experiments where the pellets were reduced to 60 pct, the dripping also varied significantly between the basic fluxed and the other types of pellets. The meltdown of the pellets reduced to 80 pct seems to be controlled by the metallic iron shell. In the pellets reduced to 60 pct, it appears that both the metallic iron and the liquid slag determine the meltdown.

Mixed burden softening and melting phenomena in blast furnace operation

The cohesive zone in the blast furnace (BF) is largely affected by the high temperature properties of the ferrous burden. Lowering and minimising the width of this zone will increase the productivity and performance of the BF. Recently part of the BF ferrous burden has been replaced by direct reduced iron (DRI) and hot briquetted iron (HBI). The objective of the present work is to expand the current understanding of softening and melting (SM) mechanism of ferrous raw materials including DRI, HBI, pellets, lump ore and mixed burdens. A small scale deformation under load experiment was designed to examine the interaction of ferrous burdens. The SM tests were conducted with ferrous burdens in different combinations and parameters such as bed contraction, pressure loss, reduction degree, etc. were measured. In addition, the process was visualised using X-ray fluoroscopy. There were microstructural differences between the ferrous materials which governed the initial compaction of bed. The softening of the single burdens of DRI and HBI occurs owing to softening of iron phase. In mixed burdens composed of DRI and pellets/ lump ore, initial deformation is not affected by the presence of DRI; however the melting of the bed is dependent on the melting of DRI indicating its dominance over other burden components at later stages of deformation. The change in reduction degree between SM temperatures was found to be small.

Thursday, 4 August 2011

HOW A BLAST FURNACE WORKS


Introduction
The purpose of a blast furnace is to chemically reduce and physically convert iron oxides into liquid iron called "hot metal". The blast furnace is a huge, steel stack lined with refractory brick, where iron ore, coke and limestone are dumped into the top, and preheated air is blown into the bottom. The raw materials require 6 to 8 hours to descend to the bottom of the furnace where they become the final product of liquid slag and liquid iron. These liquid products are drained from the furnace at regular intervals. The hot air that was blown into the bottom of the furnace ascends to the top in 6 to 8 seconds after going through numerous chemical reactions. Once a blast furnace is started it will continuously run for four to ten years with only short stops to perform planned maintenance. 

The Process


Iron oxides can come to the blast furnace plant in the form of raw ore, pellets or sinter. The raw ore is removed from the earth and sized into pieces that range from 0.5 to 1.5 inches. This ore is either Hematite (Fe2O3) or Magnetite (Fe3O4) and the iron content ranges from 50% to 70%. This iron rich ore can be charged directly into a blast furnace without any further processing. Iron ore that contains a lower iron content must be processed or beneficiated to increase its iron content. Pellets are produced from this lower iron content ore. This ore is crushed and ground into a powder so the waste material called gangue can be removed. The remaining iron-rich powder is rolled into balls and fired in a furnace to produce strong, marble-sized pellets that contain 60% to 65% iron. Sinter is produced from fine raw ore, small coke, sand-sized limestone and numerous other steel plant waste materials that contain some iron. These fine materials are proportioned to obtain a desired product chemistry then mixed together. This raw material mix is then placed on a sintering strand, which is similar to a steel conveyor belt, where it is ignited by gas fired furnace and fused by the heat from the coke fines into larger size pieces that are from 0.5 to 2.0 inches. The iron ore, pellets and sinter then become the liquid iron produced in the blast furnace with any of their remaining impurities going to the liquid slag.
The coke is produced from a mixture of coals. The coal is crushed and ground into a powder and then charged into an oven. As the oven is heated the coal is cooked so most of the volatile matter such as oil and tar are removed. The cooked coal, called coke, is removed from the oven after 18 to 24 hours of reaction time. The coke is cooled and screened into pieces ranging from one inch to four inches. The coke contains 90 to 93% carbon, some ash and sulfur but compared to raw coal is very strong. The strong pieces of coke with a high energy value provide permeability, heat and gases which are required to reduce and melt the iron ore, pellets and sinter.
The final raw material in the ironmaking process in limestone. The limestone is removed from the earth by blasting with explosives. It is then crushed and screened to a size that ranges from 0.5 inch to 1.5 inch to become blast furnace flux . This flux can be pure high calcium limestone, dolomitic limestone containing magnesia or a blend of the two types of limestone.
Since the limestone is melted to become the slag which removes sulfur and other impurities, the blast furnace operator may blend the different stones to produce the desired slag chemistry and create optimum slag properties such as a low melting point and a high fluidity.
All of the raw materials are stored in an ore field and transferred to the stockhouse before charging. Once these materials are charged into the furnace top, they go through numerous chemical and physical reactions while descending to the bottom of the furnace.
The iron ore, pellets and sinter are reduced which simply means the oxygen in the iron oxides is removed by a series of chemical reactions. These reactions occur as follows:
1) 3 Fe2O3 + CO = CO2 + 2 Fe3O4
Begins at 850° F
2) Fe3O4 + CO = CO2 + 3 FeO
Begins at 1100° F
3) FeO + CO = CO2 + Fe
     or
     FeO + C = CO + Fe
Begins at 1300° F
At the same time the iron oxides are going through these purifying reactions, they are also beginning to soften then melt and finally trickle as liquid iron through the coke to the bottom of the furnace.
The coke descends to the bottom of the furnace to the level where the preheated air or hot blast enters the blast furnace. The coke is ignited by this hot blast and immediately reacts to generate heat as follows:
C + O2 = CO2 + Heat
Since the reaction takes place in the presence of excess carbon at a high temperature the carbon dioxide is reduced to carbon monoxide as follows:
CO2+ C = 2CO
The product of this reaction, carbon monoxide, is necessary to reduce the iron ore as seen in the previous iron oxide reactions.
The limestone descends in the blast furnace and remains a solid while going through its first reaction as follows:
CaCO3 = CaO + CO2
This reaction requires energy and starts at about 1600°F. The CaO formed from this reaction is used to remove sulfur from the iron which is necessary before the hot metal becomes steel. This sulfur removing reaction is:
FeS + CaO + C = CaS + FeO + CO
The CaS becomes part of the slag. The slag is also formed from any remaining Silica (SiO2), Alumina (Al2O3), Magnesia (MgO) or Calcia (CaO) that entered with the iron ore, pellets, sinter or coke. The liquid slag then trickles through the coke bed to the bottom of the furnace where it floats on top of the liquid iron since it is less dense.
Another product of the ironmaking process, in addition to molten iron and slag, is hot dirty gases. These gases exit the top of the blast furnace and proceed through gas cleaning equipment where particulate matter is removed from the gas and the gas is cooled. This gas has a considerable energy value so it is burned as a fuel in the "hot blast stoves" which are used to preheat the air entering the blast furnace to become "hot blast". Any of the gas not burned in the stoves is sent to the boiler house and is used to generate steam which turns a turbo blower that generates the compressed air known as "cold blast" that comes to the stoves.
In summary, the blast furnace is a counter-current realtor where solids descend and gases ascend. In this reactor there are numerous chemical and physical reactions that produce the desired final product which is hot metal. A typical hot metal chemistry follows:
Iron (Fe)
= 93.5 - 95.0%
Silicon (Si)
= 0.30 - 0.90%
Sulfur (S)
= 0.025 - 0.050%
Manganese (Mn)
= 0.55 - 0.75%
Phosphorus (P)
= 0.03 - 0.09%
Titanium (Ti)
= 0.02 - 0.06%
Carbon (C)
= 4.1 - 4.4%
The Blast Furnace Plant


Now that we have completed a description of the ironmaking process, let s review the physical equipment comprising the blast furnace plant.
There is an ore storage yard that can also be an ore dock where boats and barges are unloaded. The raw materials stored in the ore yard are raw ore, several types of pellets, sinter, limestone or flux blend and possibly coke. These materials are transferred to the "stockhouse/hiline" (17) complex by ore bridges equipped with grab buckets or by conveyor belts. Materials can also be brought to the stockhouse/hiline in rail hoppers or transferred from ore bridges to self-propelled rail cars called "ore transfer cars". Each type of ore, pellet, sinter, coke and limestone is dumped into separate "storage bins" (18). The various raw materials are weighed according to a certain recipe designed to yield the desired hot metal and slag chemistry. This material weighing is done under the storage bins by a rail mounted scale car or computer controlled weigh hoppers that feed a conveyor belt. The weighed materials are then dumped into a "skip" car (19) which rides on rails up the "inclined skip bridge" to the "receiving hopper" (6) at the top of the furnace. The cables lifting the skip cars are powered from large winches located in the "hoist" house (20). Some modern blast furnace accomplish the same job with an automated conveyor stretching from the stockhouse to the furnace top.
At the top of the furnace the materials are held until a "charge" usually consisting of some type of metallic (ore, pellets or sinter), coke and flux (limestone) have accumulated. The precise filling order is developed by the blast furnace operators to carefully control gas flow and chemical reactions inside the furnace. The materials are charged into the blast furnace through two stages of conical "bells" (5) which seal in the gases and distribute the raw materials evenly around the circumference of the furnace "throat". Some modern furnaces do not have bells but instead have 2 or 3 airlock type hoppers that discharge raw materials onto a rotating chute which can change angles allowing more flexibility in precise material placement inside the furnace.
Also at the top of the blast furnace are four "uptakes" (10) where the hot, dirty gas exits the furnace dome. The gas flows up to where two uptakes merge into an "offtake" (9). The two offtakes then merge into the "downcomer" (7). At the extreme top of the uptakes there are "bleeder valves" (8) which may release gas and protect the top of the furnace from sudden gas pressure surges. The gas descends in the downcomer to the "dustcatcher", where coarse particles settle out, accumulate and are dumped into a railroad car or truck for disposal. The gas then flows through a "Venturi Scrubber" (4) which removes the finer particles and finally into a "gas cooler" (2) where water sprays reduce the temperature of the hot but clean gas. Some modern furnaces are equipped with a combined scrubber and cooling unit. The cleaned and cooled gas is now ready for burning.
The clean gas pipeline is directed to the hot blast "stove" (12). There are usually 3 or 4 cylindrical shaped stoves in a line adjacent to the blast furnace. The gas is burned in the bottom of a stove and the heat rises and transfers to refractory brick inside the stove. The products of combustion flow through passages in these bricks, out of the stove into a high "stack" (11) which is shared by all of the stoves.
Large volumes of air, from 80,000 ft3/min to 230,000 ft3/min, are generated from a turbo blower and flow through the "cold blast main" (14) up to the stoves. This cold blast then enters the stove that has been previously heated and the heat stored in the refractory brick inside the stove is transferred to the "cold blast" to form "hot blast". The hot blast temperature can be from 1600°F to 2300°F depending on the stove design and condition. This heated air then exits the stove into the "hot blast main" (13) which runs up to the furnace. There is a "mixer line" (15) connecting the cold blast main to the hot blast main that is equipped with a valve used to control the blast temperature and keep it constant. The hot blast main enters into a doughnut shaped pipe that encircles the furnace, called the "bustle pipe" (13). From the bustle pipe, the hot blast is directed into the furnace through nozzles called "tuyeres" (30) (pronounced "tweers"). These tuyeres are equally spaced around the circumference of the furnace. There may be fourteen tuyeres on a small blast furnace and forty tuyeres on a large blast furnace. These tuyeres are made of copper and are water cooled since the temperature directly in front of the them may be 3600°F to 4200°F. Oil, tar, natural gas, powdered coal and oxygen can also be injected into the furnace at tuyere level to combine with the coke to release additional energy which is necessary to increase productivity. The molten iron and slag drip past the tuyeres on the way to the furnace hearth which starts immediately below tuyere level.
Around the bottom half of the blast furnace the "casthouse" (1) encloses the bustle pipe, tuyeres and the equipment for "casting" the liquid iron and slag. The opening in the furnace hearth for casting or draining the furnace is called the "iron notch" (22). A large drill mounted on a pivoting base called the "taphole drill" (23) swings up to the iron notch and drills a hole through the refractory clay plug into the liquid iron. Another opening on the furnace called the "cinder notch" (21) is used to draw off slag or iron in emergency situations. Once the taphole is drilled open, liquid iron and slag flow down a deep trench called a "trough" (28). Set across and into the trough is a block of refractory, called a "skimmer", which has a small opening underneath it. The hot metal flows through this skimmer opening, over the "iron dam" and down the "iron runners" (27). Since the slag is less dense than iron, it floats on top of the iron, down the trough, hits the skimmer and is diverted into the "slag runners" (24). The liquid slag flows into "slag pots" (25) or into slag pits (not shown) and the liquid iron flows into refractory lined "ladles" (26) known as torpedo cars or sub cars due to their shape. When the liquids in the furnace are drained down to taphole level, some of the blast from the tuyeres causes the taphole to spit. This signals the end of the cast, so the "mudgun" (29) is swung into the iron notch. The mudgun cylinder, which was previously filled with a refractory clay, is actuated and the cylinder ram pushes clay into the iron notch stopping the flow of liquids. When the cast is complete, the iron ladles are taken to the steel shops for processing into steel and the slag is taken to the slag dump where it is processed into roadfill or railroad ballast. The casthouse is then cleaned and readied for the next cast which may occur in 45 minutes to 2 hours. Modern, larger blast furnaces may have as many as four tapholes and two casthouses. It is important to cast the furnace at the same rate that raw materials are charged and iron/slag produced so liquid levels can be maintained in the hearth and below the tuyeres. Liquid levels above the tuyeres can burn the copper casting and damage the furnace lining.
CONCLUSION
The blast furnace is the first step in producing steel from iron oxides. The first blast furnaces appeared in the 14th Century and produced one ton per day. Blast furnace equipment is in continuous evolution and modern, giant furnaces produce 13,000 tons per day. Even though equipment is improved and higher production rates can be achieved, the processes inside the blast furnace remain the same. Blast furnaces will survive into the next millenium because the larger, efficient furnaces can produce hot metal at costs competitive with other iron making technologies. 

RAFT FORMULA WITH COAL

Raft Temp. = 1615. - 5.75*BM + 53.3*OE + 0.76*HBTemp - PCIRate*2.3*1000000./BF

RAFT FORMULA

RAFT = 1615 + (0.76*HBT) – (5.75*Humidity) + 53.3 E

               HBT = Hot Blast Temperature   0C 
               Humidity = Grams / Nm3 
               E = Oxygen Enrichment = 79 * Oxy. Flow ( M3/hr) / Hot Blast Flow ( M3/hr)

BLAST FURNACE VIDEO 3D



BLAST FURNACE VIDEO


BLAST FURNACE VIDEO


Wednesday, 3 August 2011

BF TOP GAS FIRING

IRON CARBON PHASE DIAGRAM

CHECKPOINTS PRIOR TO COMMISSIONING

COLD TRIALS COMPLETE & OK
EQUIPMENTS TESTED OK
PRESSURE TESTING OF UTILITY LINES, STOVES AND FURNACE DONE
INSTRUMENTATION & AUTOMATION INTERLOCKS & LOGISTICS DONE
ALL UTILITY LINES ( COOLING WATER, COG,OXYGEN, NITROGEN,STEAM,COMPRESSED AIR,COREX GAS) CHARGED
SPARES AND CONSUMMABLES PROCURED IN SUFFICIENT QUANTITY
ALL WORK ORDERS FOR EQUIPMENT HANDLING & MANPOWER ISSUED
STOVE WARM UP EQUIPMENTS READY
RAW MATERIAL STOCK AND SUPPLY LINE READY
HOT METAL DISTRIBUTION LINE READY
PROCEDURE FOR COMMISSIONING READY
TEAM FOR COMMISSIONING READY

Thermal Control

This procedure describes the measure to be taken for majors changes in the thermal balance of the furnace. It is emphasised that the action describe are guidelines, and before any action is taken the recent furnace operation and process changes are to be considered.

Changes to the furnace thermal balance should be made taking the following relationship into account.

Parameter
Extent of
change
Effect on coke rate
(kg./Thm)
Time to Affect Metal Temp. (hrs)
Effect on Metal Temperature
Blast temperature
+100˚C
-5.5
5
+22.5˚C
Blast moisture
+10g/Nm³
3.5
6
-14˚C
Hot Metal Silicon
+0.1%
+2.0

-8˚C
Hot Metal Temp.
+10˚C
+2.5


Co Utilisation
+1%
-4.5
7
+18˚C
Coke Ash
+1%
+4.0

-16˚C
Slag Volume
+10kg/THM
1.2

-5˚C
Heat Flux
+2Gcal/hr
+1.0
7
-4.0˚C
Coke Rate


24

Coal Rate


12 ?

Blast Volume


5



The data is based on Redcar Furnace.
The heat content of coke is 5233Kcal/kg (90%C dry)

The normal order of priority for parameter change is:
1st      Blast moisture
2nd     Coke rate
3rd      Coal rate
4th      Blast temperature

Assume the heat content of coal is the same as for coke for small changes. ????

When assessing trends in metal quality the following time constant should be taken into account.


Gas Utilisation
Changes in CO utilisation often reflects previous parameter changes (e.g. reduced/increased coke rate) and metal temperature trends. Thus it is important to consider such changes when considering adjustment to the thermal balance based on CO utilisation. A recalibration of the top gas analyser should be initiated if there is a marked change in Eta CO which is not consistent with the current furnace operation. (is there a back up analyser ???, If there is still doubt the back up analyser used as reference, problems arise with both analysers ) Contact the laboratory and request hourly samples to be analysed.
If a change in gas utilisation is identified as an indicator of future metal quality then following should be considered.

If Eta CO shows a significant downward trend compared to the previous 8 hours (e.g. 1% lower for 4 hours or 2% lower for 2 hours) indicating a cooling trend, then the coke rate should be increased on the basis of 1% Eta CO = 4.6%Kg/THM

If Eta CO shows an upward trend then no compensation is to be applied until metal quality shows a warming trend. Then the compensation will be by blast moisture initially and may later be ‘traded’ for a decrease in fuel rate.

Reduced Blast Volume
Reduced blast volume may result in increased metal temperature. This should be taken into account when considering changes to the thermal balance.

A Racing Furnace
If the true charging rate increases above the norm and is maintained, it may result in a cooling trend. This should be taken into account when considering changes to the thermal balance.

Hot blast temperature and flame temperature
If the hot blast temperature is lower than the aim for more than 4 hours then a fuel rate equivalent change is to be made to restore the thermal input. However if by reducing the blast moisture results in a flame temperature above 2250˚C then the coal rate or coke rate should be increased instead.




Heat Flux
Heat flux may change because of the influences of raw materials quality, burden distribution or liquids removal. Significant and prolonged changes in heat flux should be compensated on the basis of 1kg/THM fuel for each 2Gcal/hr changes in heat flux. Caution should be exercised when taking action in response to heat flux – other parameter changes may affect the actual compensation required.  


Stock Sinter
Extensive use of stock sinter may lead to a warming trend in the hot metal. This is due to the moisture content of stock sinter causing a reduction in the dry weight changed. This should be taken into account when considering changes to the thermal balance.

Burdening Policy
If the burdening policy is altered then the fuel rate is to be maintained. Whilst also taking account any changes to the slag volume.

Taphole changeovers
A dip in metal quality may be observed at taphole changeovers and consequently req1uires caution when assessing quality trends at such times.