Coal Hang-up in Bowl Mill

Written by:  • Edited by: Lamar Stonecypher
Updated Jun 13, 2010
• Related Guides: Coal Fired Boilers

Depending on the quality of the coal, sometimes the smooth flow to the coal mill can be disrupted. The mill will then trip on flow protection, upsetting boiler parameters and demanding immediate operator corrective action.

Bowl mills are used for pulverizing coal in pulverized coal fired boilers. The coal to the mill is fed by a coal feeder from the coal bunker. There are many type of feeders used for coal feeding like the belt feeder which can be in volumetric or gravimetric mode, the chain link feeder, the drag feeder, etc. Row coal from the yard is sized in crushers and stored in coal bunkers. It is sometimes experienced, depending upon coal quality, that the smooth flow to the coal mill can get disrupted. The mill will trip on no coal flow protection, and such a mill trip can upset boiler parameters and require corrective action.

For taking corrective action during a coal hang-up in bowl mills, the operator will have to know the reason for such a hang up, how the plant will respond, what he has to respond to, and what the local operator will have to do. This will reduce the chance of mill trip and bring the boiler back to normal condition as early as possible.

Specific causes

The reasons for coal hang-up to mills can be many, like large raw coal size, jamming of the feeder, jamming of the coal chute from the bunker due to high moisture in the coal, foreign material at raw coal inlet to feeder, etc.

Plant responses

The boiler fuel input coming down due to coal flow hang-up the mill slowly gets unloaded. This can be inferred from the response of the boiler.

  • Mill differential pressure comes down
  • Mill outlet temperature will rise
  • Boiler steam pressure will start falling
  • No coal flow alarm will appear
  • Coal feeder and mill will trip after some time
  • Mill outlet temperature high alarm will appear

Operator responses

On seeing the changes in the operating parameters of the mill the operator will have to take corrective action.

  • Reduce the load on the boiler and inform the steam consumer accordingly
  • Maintain boiler pressure and temperature of steam
  • Start reserve mill and stabilize, if reserve mill is on maintenance, then ask local operator for the reason for hang-up and his action plan
  • Keep steam consumers informed of your action
  • Once coal flow is restored through the reserve mill or the same mill, steam consumer can be asked to increase load

Local operator responses

In this case the local operator will have to play a major role in helping the control room boiler operator by performing the following checks and deciding further course of action.

  • Check whether the hot air and cold air gates are closed, if not then close both
  • Check hot air to raw coal and feeder is closed, if not close this
  • Close the raw coal feeder inlet gate if not already closed
  • After making sure all the above are closed, open the inspection door of the mill
    • Check if the coal pipe from feeder to mill is clear and make sure they are made clear
    • Check raw coal feeder and if chocked then get it cleaned
    • Check the raw coal feeder shear pin and replace if needed
    • Now operate on no load and check for smooth running
    • Check the coal chute from bunker to feeder is clear, that is from the closed feeder inlet gate onwards
  • Check the bunker for coal, if empty organize for filling immediately
  • If mill has any remnant materials then clean the mill and restart the mill and check for smooth operation
  • Now clear the mill for resuming operation

Coal Mill Hang-up

Coal Hang-up in Bowl Mill

Comments

Showing all 11 comments
 
Dr V T Sathyanathan Sep 23, 2010 8:31 PM
Reply to Krishnan
Choking is not uncommon while handling high moisture. Look at both bunker bottom transition and the angle of the chute at the outlet of the bunker. This plays an important role in choking of coal bunker; both have to be near vertical. This requires detailed study before final conclusions.
krishnan Sep 21, 2010 6:28 AM
coal bunker choking
We are constantly facing problems related to coal bunker choking. The bunker opening is about 1 feet dia. The choking issue is leading to starvation of our mills forcing us to throttle the plant. What we understand is that the coal particles get struck on the walls preventing free flow of coal into the mill. It has been raining for soem time and the coal mositure is about 20% TM. We also have lots of fines in the coal. can you pl suggest a solution to this problem
dhinesh Jul 29, 2010 7:18 AM
thanku sir.
thanks for your response sir.
sir,
you are saying,we can use bowl mill for lignite.there is no much difference to replace beater mill by bowl mill based on boiler efficiency, power consumption and drying capacity.
if i'm using flue gas to dry the lignite and beater mill to pulverize it.
dhinesh Jul 27, 2010 12:01 AM
pulveriser re
thank you sir.
Dr V T Sathyanathan Jul 23, 2010 1:32 AM
Reply to Dhinesh for both questions
moisture content coal(lignite)? thanks in advance!!
Beater mills have ability to handle high inlet-air/flue gas temperatures, plus the return of dried classified rejects to the incoming raw feed, makes it an excellent dryer. However wear on the grinding elements produces a rapid drop-off in product fineness. Normally lignite has low ash and also does not require in true sense pulverization to very high fineness, the particle size can be upto1 mm. Hence capacity drop is not a very big issue. In case of bowl very high moisture requires high inlet temperature and has to operate with high fuel air ratio. Many power plants abroad use bowl mill for lignite. It is more a question of how you want to do, the capacity of the plant, the space availability, boiler efficiency levels, etc. In my opinion there is no limitation per say in using the bowl mill for lignite with high moisture. These mills generally have a power consumption of about 8 to 12 kWh/t when compared to 15 to 25kWh/t for ball tube mill.
Dr V T Sathyanathan Jul 23, 2010 1:31 AM
Reply to S V Waghmode
I know there are both nucleonic, vibration pick-up and ultrasonic types are used for this application. But the suppliers I have no data now. Let me see if I get then shall put it up again.
dhinesh Jul 20, 2010 2:10 AM
beater mill
thank u sir. but for high moisture content why we go for beater mill?why cant we go for slow speed mills like ball or bowl mill?
what is the additional feature beater mill have over bowl mill to accommodate high moisture content coal(lignite)?
thanks in advance!!
dhinesh Jul 19, 2010 4:31 AM
RE: Coal Hang-up in Bowl Mill
sir,
how do u say that for high moisture content high speed mills (beater / hammer)are
the best one.to dry the lignite we are using flue gas.then why cant we go for slow speed mills like ball or bowl etc.any problem is there if we replace it with bowl mill.
svwaghmode Jul 18, 2010 8:37 AM
pulveriser re
Hello dinesh
lignite has high moisture so beater or hammer mill found to be best option.
dhinesh Jul 17, 2010 1:48 AM
pulverizer
sir,
i'm dhinesh working in coal based thermal power plant.i have a doubt related to pulverizer.why cant we use a mill other than beater mill for pulverizing lignite?
what's the power consumption of beater mill(210T/hr) and other mills for handling the same capacity?can we use bowl mill for lignite fired boilers?can u help me!!
S V Waghmode Feb 10, 2010 10:32 AM
coal bunker chute choke alarm
Can u suggest some instrument which will show No Coal Flow to Feeder alarm due to coal bunker chute choke or any other reason. This will make operator alert in above case.
 
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