Coal Analysis for Boiler Designers

Written by:  • Edited by: Lamar Stonecypher
Published Jul 3, 2009
• Related Guides: Fuel

Hydrocarbon fuels are the major source of energy for power and process steam generation, and coal takes a major share in this. Boiler furnace design will depend more on fuel characteristics, and further heat transfer surface sizing will depend on furnace outlet temperature.

The world's thermal power is mainly dependent on coal as its fuel. When designing a boiler, fuel analysis plays a major role. The performance of the boiler, and ultimately the entire unit, can change considerably if the coal being used is substantially different from that for which the boiler was designed.

What is fuel?

  • Any combination of organics and inorganic material which during chemical reaction or transformation gives out large amount of heat is called fuel
  • Fuel can be hydrocarbon fuel and non-hydrocarbon
  • Industrial fuels have heat values from as low as 500 kcal/kg to as high as 11000 kcals/kg

Heat generated by fuel is used a boiler to generate steam for process, power generation, and a variety of other applications. The chemical characteristics of the fuel decide many aspects of boiler design. The boiler designed for gas fuel will have the smallest furnace size, and the boiler designed for coal will have the biggest size.

Why is coal different?

  • All fuels are hydrocarbons
  • Gas and oil have defined hydrocarbons and structure, which means C & H in fuel does not vary much
  • Coal is a heterogeneous fuel and has only an assumed structure – C & H vary highly
  • C & H in Coal can be only be known if you do an ultimate analysis, and the way in which these hydrocarbon behave can be different from one coal to the other. This will depend on its reactivity and formation.
  • Formation of coal has vast impact on boiler design; the Gondwana coals are different from American and European. (Coal formation theories).

Why is consistency in hydrocarbon important for boiler performance?

  • It starts from combustion air calculation; the carbon hydrogen ratio decides the quantity of combustion air.
  • Flame temperature is dictated by the chemical composition of the fuel, and this changes the furnace behavior.
  • The completion of combustion is another very important factor in boiler design. This will depend on how the hydrocarbon rings are formed and bonded. If the coal burns slowly requiring more residence time then the SH and RH (superheater and reheater) behavior changes when compared to the fast burning coal. This will lead to large injection in SH and/or RH which will reduce the life of the tubes and also reduce boiler efficiency.
  • The amount of unburned material in fly ash and bottom ash of the boiler can change, and, if it increases will increase fuel requirement, maybe only marginally.
  • Lack of consistency can lead to loss of the capability to generate when the ash level increases beyond a threshold of the fuel preparation system capacity. This can also lead to limitations on the fuel handling system.

Major effects of fuel on boiler design

  • A wide range of coal properties can lead to oversized pulverizing/firing equipment which will in turn lead to a limitation on turn down and a possible increase in auxiliary power consumption. This will also increase the furnace size and the SH and RH will need to be sized properly, which can be difficult at times, to get the rated outlet temperature.
  • Oversizing of pulverizers and air heaters to handle occasionally high moisture coals will require excessive tempering air when handling normal moisture coals. Ultimately all these will result in higher gas outlet temperature, reducing the boiler efficiency.
  • The behavior of the ash during the combustion process and managing the coal-ash are the major issues in boiler design. Deposition and slagging, heat transfer upsets, and fouling in convection passages are some of the major issues to be dealt during operation of the boiler.

Steam generator performance is greatly influenced by the coal/ash properties. Changes in coal property result in efficiency variation and the designer may not be able to demonstrate the guarantees. This can also result in changes in power consumption, load limitations, boiler availability loss due to slagging and fouling, tube failure increases, and plant heat rate reduction. There are known and unknowns with coal during combustion. The known are the coal Proximate, Ultimate, Calorific Value, HGI, and Ash analysis. The unknown are Petrographic analysis, Reactivity, Slagging and fouling analysis, etc. All unknown become known only after the combustion of coal in the boiler furnace and at the cost of boiler performance.


Comments

Showing all 25 comments
 
Dr V T Sathyanathan Oct 11, 2011 4:19 AM
Reply to Ramesh
This is difficult one to answer now, as not many super critical boilers are operating in India, so my experience is limited. But what are you trying to look for, one of the super critical boiler being commissioned had air pre-heater fire, another is reported to have high combustibles in ash leading to higher carbon loss and so lower operating efficiency, and may be some more. All these are not due to supercritical in nature but happen in other boilers too.
Dr V T Sathyanathan Oct 11, 2011 4:19 AM
Reply to Ramesh
I am not very clear what you are looking for, in super critical boilers the pressure is above the critical pressure, the SH temperature is normally kept higher than 540, the most critical factor to be taken care is the DNB in water walls, the overall cycle efficiency is higher depending upon pressure & temperature, etc.
Dr V T Sathyanathan Oct 11, 2011 4:19 AM
Reply to Ramesh
Please see my posting on steam blowing, link given below.
http://www.brighthub.com/engineering/mechanical/articles/71650.aspx
Dr V T Sathyanathan Oct 11, 2011 4:18 AM
Reply to Ramesh
If the GCV of the coal changes from design value within 10% normally there is no change in the boiler performance, except you either handle less kgs of coal when GCV goes up and higher when GCV comes down. But when it changes very widely then it is difficult to say that these are the changes. Apart from change in coal to be handled and prepared changes, depending on the reactivity, ash composition, excess air etc. Normally problems like deposition on water walls, high superheater injection, and high exit gas temperature are the main thing which happens when the coal quality is poor that is very low GCV. When it is a high GCV, then the FOT can be lower due to which the steam temperature at the SH outlet can be low. Due to all these the boiler efficiency can be lower.
ramesh Oct 10, 2011 2:58 AM
SC commonising problem
DEAR SIR
1) SUPER CRTICAL BOILER FACING ANY COMMISSIONING PROBLEM ? ANY PROBLEM IS THERE GIVE SOME SUGGESTION SIR
ramesh Oct 10, 2011 2:56 AM
boiler design
What are the main factors to design the super crtical boiler ?
ramesh Oct 10, 2011 2:50 AM
steam blowing
dear sir ,

steam blowing operation what is allowable velocity ?
ramesh Oct 10, 2011 2:43 AM
boiler design
dear sir,

our boiler design c.v 4300 kcal /kg GCV coal ,suppose that value of gcv some time is higher than orginal value or some time lower than GCV.that time what will be the effect of boiler design .
effects is there what will be the effect. i am waiting for your favorable reply.
Dr V T Sathyanathan Feb 16, 2011 2:19 AM
Replt to Ganesh
If you are talking about coal and oil then this cannot be done. If it is gas we can mix in the required proportion the C/H ratio can be altered. About ultimate analysis I am not clear what you want.
Ganesh Jan 31, 2011 9:51 AM
C/H ratio variation
Dear Sir,
How C/H ratio is varied keeping the HHV constant. As it the C/H ratio can be increased by either increasing H with C constant or by decreasing C and keeping H constant. Can you please explain which parameter to be changed and also let us know how to achieve the total of ultimate anlaysis 100 %.
Dr V T Sathyanathan Dec 26, 2010 10:30 AM
Reply to Sivakumar
Primary air quantity is predicted based on the organics in coal and calculating the total air required. About 30% is the PA flow. The main function of PA flow is to give oxygen in the primary region of the flame, where ignition and flame stabilization take place. The temperature of PA is determined depending on the moisture in coal. The transport of fuel from ill to furnace is the next main requirement of PA, this quantity is determined based on the mill size and settling velocity of the fuel particle. However this quantity will depend on quantity of fuel milled, so many mill designers decide this based on mill size and fuel pipe used for the mill. After having said this, it is not that each time it is calculated but are kept in form of selection chat by the mill designers.
Please read my article on combustion optimization where I have said about the way in which the PA flow can be maintained to the optimal level for a bowl mill when firing high ash coal.

http://www.brighthub.com/engineering/mechanical/articles/37755.aspx?p=2
SIVAKUMAR Dec 17, 2010 1:03 PM
Primary Air %
Sir,
In pulverized coal fired boiler, Primary air flow is depends on
1. Air required to evaporate the Moisture in coal or
2. Air required to carry the fuel

Are there any way to predict the exact quantity of air required as primary and forced draft?
Dr V T Sathyanathan Dec 16, 2010 8:46 PM
Reply to Sivakumar
To my knowledge there is no formula but all are based on experience and selection chats. MOT has to ensure that the particles are dry enough not to agglomerate, it is seen this is around 60 to 65 deg C. So depending upon the moisture in coal the mill inlet temperature is selected. However the high volatile mater coal poses a problem of mill fires if the mill outlet temperature is maintained higher than required which varies, but normally around 65 degree C.
SIVAKUMAR Dec 8, 2010 12:48 PM
Mill Outlet air temperature
Please explain any formula with pertain to volatile matter and mill outlet temperature. kindly suggest how to decide the MOT for particular coal.?
Dr V T Sathyanathan Dec 2, 2010 10:08 AM
Reply to Shanil Nambiar
Let me plan and write on this soon.
SHANIL NAMBIAR Dec 2, 2010 4:30 AM
Coal quality
Sir, can you provide me any information regarding the topic"implications of coal quality on boiler design".please put your interest on it..
Ganesh Dhawas Nov 2, 2010 4:11 AM
Drum level control
What are the compensations for 1-element, 2-element, 3-element & 5-element drum level control in boilers?
Dr V T Sathyanathan Oct 20, 2010 6:23 AM
Reply to Babar Khan
Coal water slurry fuel is a liquid and can be fired like fuel oil. The economics part depends on what all things are important to you. If liquid firing is the only alternate to you then CWS will be a comparable option. No doubt that PC is cheaper under normal circumstances.
Babar Khan Oct 19, 2010 1:29 AM
Coal Slurry Fuels
How would you compare Coal Slurry Fuel with ordinary Pulverised Coal? If one needs to convert the RFO fired boilers to any of the coal derivatives i.e. PC or CWS, economics seems to favor PC, then why world came up with CWS??
Dr V T Sathyanathan Jun 26, 2010 12:48 AM
Reply to MV Balachandra
The maximum mill inlet temperature will have to be designed based on the maximum moisture expected in coal.
Dr V T Sathyanathan Jun 26, 2010 12:47 AM
Reply to Shailendrasharma
Operating coal mills with 100 degree C has to be decided very carefully. This can lead to mill fire if VM increases during operation due to coal change. I would prefer to operate with 90 degree C outlet temperature. If we have to reduce the increasing outlet temperature go in for tempering air. Using tempering air does not increase carbon loss, but increases the dry gas loss, due to the fact that the tempering air bypasses air pre-heater.
MV Balachandra Jun 25, 2010 9:32 PM
Mill inlet air temperature
What is the max mill inlet air temperature is acceptable.
shailendrasharma May 27, 2010 4:59 AM
Coal ait mixture outlet temperature at coal mills.
Dear Sir,
If I have a choise to operate at temperature of fuel air mixture around 90-100 deg,C .Which condition is better
1.using tempering air to control temperature around 90 Deg.C
2.operating at 100 deg.C with zero tempering air.
Does tempering air causes increase in un-burnt carbon losses.
Regards
Dr V T Sathyanathan Mar 28, 2010 12:25 AM
Mill inlet air temperature – Reply to Rajesh Kumar
Mill inlet temperature depends on the coal moisture. During boiler design stage depending upon the design coal specified the boiler designers select the economizer and air pre-heater size in such a way to get the desired mill inlet temperature required to dry to a condition acceptable. This is achieved by maintaining the mill outlet temperature of around 70 degree C (65 to 90 degree C). This again will depend also on the volatile mater in coal.

So I would like to tell you that all this will depend upon how close you are operating under design condition using design coal. There is nothing like a mill inlet temperature.
rajesh kumar Mar 26, 2010 2:17 AM
Mill inlet air temperature
What is the max mill inlet air temperature is acceptable.
 
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