Thank you for the feedback, very much appreciate it! By the way, I have been working on new training material you might be interested to see... ua-cam.com/video/rd0VQDoIOI8/v-deo.html&
Thank you for the feedback Mohan! Yes, in case I can be of some help do not hesitate to contact me again. For your information I am very busy at the moment and may take quite some time to come back with an adequate response. Many greetings, Fred
Hello, Thank you for the email and request. All is fine here but unfortunately I have no time to produce new videos at the moment. I cannot tell you when I will be able to produce them, sorry about that. Keep well and healthy! Fred
Great video. Very informative. I am having an issue with my Kiln analyzer. The CO2 levels are high and there is too much condensation in the analyzer which brings the CO2 levels up. Any advice? Thank you.
Sorry, I just noticed your comment now... I guess that you mean CO. Before entering the analyzer the gas sample should go through a dehydrator. I know there are many models in the market but I would not be in the position to suggest one or another. Muchos saludos, Fred
To calculate the clinker production you use the so called "clinker factor" or raw meal factor. This factor is based on the LOI or "loss on ignition", which considers mainly how much CO2 is released from you calcium carbonate. The factor also considers the dust "lost" or the dust which is not recovered from the 1st stage of your preheater tower. The LOI can be calculate with the chemical composition of your raw meal. The dust loss, cannot be calculated, unfortunately. In other words if you feed 100 t/h to the kiln and you have a clinker factor of 1.56 then, in theory you will produce 64 t/h of clinker... But not all the kiln feed will go through the kiln, because of the dust loss. The only good and precise way to know your real clinker factor (which will include dust loss) is to measure and weight the actual clinker production during a defined amount of time (ideally 8 or more hours), with the kiln running very stable and with the same feed. A rule of thumb to know your clinker production (very rough estimate) is to multiply the kiln feed t/h x 15 = tons of clinker per day. In you case, your system would produce 8200 tons / day or 340 t/h. This would be a very approximate 1.60 clinker factor. I hope this helps.... let me know please! Regards, Fred
@@vbrcement3666 if the free lime in clincker is more than 2% or less than 0.80% then how will it effect grinding efficiency ? I have mail you this question but due to some issue it remains unsent.. I apologize for that ..
Sir reduce ph draft and flow But increase kiln coal firing And also kiln rpm must be increase Kc firing 30 to 35 % Pc firing 70 to 75% maintad I feel if kiln coal is not sufficient then That time esp temperature should be gradually increased
Respected effort, thanks Sir.
Thank you for the feedback, very much appreciate it!
By the way, I have been working on new training material you might be interested to see...
ua-cam.com/video/rd0VQDoIOI8/v-deo.html&
EXCELLENT INFORTMATION SIR. I WILL TRY TO SHARE MY PLANT SCREEN SHOTS. MY PLANT IS ALSO LOOKS DEFICIENT LIKE WHAT ALL YOU SAID FOR THIS PLANT.
Thank you for the feedback Mohan! Yes, in case I can be of some help do not hesitate to contact me again. For your information I am very busy at the moment and may take quite some time to come back with an adequate response.
Many greetings, Fred
Hi sir.
we waiting you to share new videos for long time
We hope you're good and healthy
Hello,
Thank you for the email and request. All is fine here but unfortunately I have no time to produce new videos at the moment. I cannot tell you when I will be able to produce them, sorry about that.
Keep well and healthy!
Fred
Hai
Good work Mr. Fred
I am glad you enjoyed the video and profit from it!
Thank you for the positive response.
Great video. Very informative. I am having an issue with my Kiln analyzer. The CO2 levels are high and there is too much condensation in the analyzer which brings the CO2 levels up. Any advice? Thank you.
Sorry, I just noticed your comment now...
I guess that you mean CO.
Before entering the analyzer the gas sample should go through a dehydrator. I know there are many models in the market but I would not be in the position to suggest one or another.
Muchos saludos, Fred
if the klin feed is 545 ton per hour what will be the clincker output or clincker produce and how it is calculated.. please can you tel me
To calculate the clinker production you use the so called "clinker factor" or raw meal factor.
This factor is based on the LOI or "loss on ignition", which considers mainly how much CO2 is released from you calcium carbonate. The factor also considers the dust "lost" or the dust which is not recovered from the 1st stage of your preheater tower.
The LOI can be calculate with the chemical composition of your raw meal. The dust loss, cannot be calculated, unfortunately.
In other words if you feed 100 t/h to the kiln and you have a clinker factor of 1.56 then, in theory you will produce 64 t/h of clinker... But not all the kiln feed will go through the kiln, because of the dust loss.
The only good and precise way to know your real clinker factor (which will include dust loss) is to measure and weight the actual clinker production during a defined amount of time (ideally 8 or more hours), with the kiln running very stable and with the same feed.
A rule of thumb to know your clinker production (very rough estimate) is to multiply the kiln feed t/h x 15 = tons of clinker per day. In you case, your system would produce 8200 tons / day or 340 t/h. This would be a very approximate 1.60 clinker factor.
I hope this helps.... let me know please!
Regards, Fred
@@vbrcement3666sir can I get your contact details
Good
If u observe kiln capacity and margin
And also pre heater capacity also
If kin feed is 250tph then clinker output is
Roughly 153 is comming
can i contact you personally i have some doubt to be cleared it will be great pleasure for me
Yes, of course, you can email me directly at
vbrcement@gmail.com
and we can start from there...
And ... no contacts from your side, is it all right?
@@vbrcement3666 i have already mail you sir
@@AlokSharma-qqwwee
Then I am not sure what you mean when you ask if you can contact me personally.
Please clarify what you need.
@@vbrcement3666 if the free lime in clincker is more than 2% or less than 0.80% then how will it effect grinding efficiency ? I have mail you this question but due to some issue it remains unsent..
I apologize for that ..
Kf is 250 tph
Clinker approximately 3600 tonnes to 3700 tonnes clinker per day is comming
Sir reduce ph draft and flow
But increase kiln coal firing
And also kiln rpm must be increase
Kc firing 30 to 35 %
Pc firing 70 to 75% maintad
I feel if kiln coal is not sufficient then
That time esp temperature should be gradually increased
Air balance and heat balance is not
Correct properly